JPH03164419A - Treatment of gaseous carbon dioxide - Google Patents
Treatment of gaseous carbon dioxideInfo
- Publication number
- JPH03164419A JPH03164419A JP1300806A JP30080689A JPH03164419A JP H03164419 A JPH03164419 A JP H03164419A JP 1300806 A JP1300806 A JP 1300806A JP 30080689 A JP30080689 A JP 30080689A JP H03164419 A JPH03164419 A JP H03164419A
- Authority
- JP
- Japan
- Prior art keywords
- carbon dioxide
- clathrate
- atmosphere
- gas
- seawater
- 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.)
- Pending
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 102
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 51
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 45
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000013535 sea water Substances 0.000 claims abstract description 12
- 239000013078 crystal Substances 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- 238000002485 combustion reaction Methods 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 10
- 238000007789 sealing Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 7
- 239000007787 solid Substances 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 2
- 239000000567 combustion gas Substances 0.000 abstract 3
- 239000002699 waste material Substances 0.000 abstract 3
- 230000000717 retained effect Effects 0.000 abstract 1
- 239000002803 fossil fuel Substances 0.000 description 6
- 239000010454 slate Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000007711 solidification Methods 0.000 description 3
- 230000008023 solidification Effects 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 235000014653 Carica parviflora Nutrition 0.000 description 1
- 241000243321 Cnidaria Species 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000887 hydrating effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000010587 phase diagram Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000004233 talus Anatomy 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
Landscapes
- Treating Waste Gases (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Carbon And Carbon Compounds (AREA)
Abstract
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処理方法に関し、特に燃焼排ガス中
の炭酸ガスを処理して大気へ排出される炭酸ガスを低減
する方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for treating carbon dioxide gas, and more particularly to a method for treating carbon dioxide gas in combustion exhaust gas to reduce the amount of carbon dioxide gas discharged into the atmosphere.
発電用ボイラ、産業用ボイラなど化石燃料の燃焼により
発生する排ガス中の炭酸ガスは、従来そのま\大気中に
放出されており、燃焼排ガスから炭酸ガスを分離・回収
を行い排出するガス中の炭酸ガス量(濃度)を低減する
目的の工業的手段は殆んど請じられていない現状である
。Conventionally, carbon dioxide in the exhaust gas generated by the combustion of fossil fuels such as power generation boilers and industrial boilers is released into the atmosphere as is. At present, there is almost no demand for industrial means for reducing the amount (concentration) of carbon dioxide gas.
大気中の炭酸ガス濃度は1960年=315ppm ,
1 9 7 0 : 3 2 5 ppm , 1
9 8 0年:33 5 9pmと徐々に増加し現在は
約350ppmと言われている。炭酸ガス濃度増加の原
因は木材伐採、森林の砂漠化、サンゴ礁の破壊あるいは
人口増加を含めた種々の要因の総合結果と考えられるが
、石炭、石油など化石燃料の使用量の経年増加と炭酸ガ
ス濃度の経年増加傾向が類似することから、化石燃料燃
焼による炭酸ガス排出が大気中濃度上昇の大きな原因で
あると推論されている。The concentration of carbon dioxide in the atmosphere was 315 ppm in 1960.
1970: 325 ppm, 1
In 1980, it gradually increased to 3359 pm and is now said to be about 350 ppm. The increase in carbon dioxide concentration is thought to be the result of a combination of various factors, including logging, desertification of forests, destruction of coral reefs, and population growth. Since the trends in the concentration increase over time are similar, it is inferred that carbon dioxide emissions from fossil fuel combustion are a major cause of the increase in atmospheric concentration.
大気中の炭酸ガスの増加は大気の温度が上昇し、気候(
地表)の温暖化あるいは温室効果を招き、その結果、南
極氷山溶解、海水温上昇、海水位上昇、森林砂漠化、゛
食糧不足などを順次誘発し、将来の人類の生命が危ぶま
れることとなる。化石燃料を現状のま\燃やし続け、排
ガス中の炭酸ガスをそのま\排出すれば、今後確実に大
気中の炭酸ガス濃度が増加すると予測できる。The increase in carbon dioxide gas in the atmosphere causes the temperature of the atmosphere to rise and the climate (
This will lead to global warming (on the earth's surface) or the greenhouse effect, which in turn will lead to melting of Antarctic icebergs, rising ocean temperatures, rising sea levels, desertification of forests, food shortages, etc., endangering the future of human life. . If we continue to burn fossil fuels at the current rate and emit carbon dioxide in exhaust gas as is, we can predict that the concentration of carbon dioxide in the atmosphere will definitely increase in the future.
本発明は大気中の炭酸ガス増加現象を低減させるため、
化石燃料の燃焼排ガスからそれに含まれる炭酸ガスの全
量または一部を分離・回収して再び大気中に放出しない
ように固定する方法を提供しようとするものである。In order to reduce the phenomenon of increase in carbon dioxide gas in the atmosphere, the present invention
The present invention aims to provide a method for separating and recovering all or part of carbon dioxide contained in fossil fuel combustion exhaust gas and fixing it so that it will not be released into the atmosphere again.
本発明は燃焼排ガスなど大気中に放出する炭酸ガス濃度
を低減させる方法において、濃縮分離した炭酸ガスを海
水と混合させ低温、かつ加圧下の化学反応により水の結
晶の中に炭酸ガス分子をとり込んだタラスレート永和物
を生成させ、これを深海底へ圧力輸送するかあるいはコ
ンテナに封入して海洋投棄することを特徴とする炭酸ガ
スの処理方法である。The present invention is a method for reducing the concentration of carbon dioxide emitted into the atmosphere, such as combustion exhaust gas, by mixing concentrated and separated carbon dioxide with seawater, and creating carbon dioxide molecules in water crystals through a chemical reaction at low temperatures and under pressure. This is a method for processing carbon dioxide gas, which is characterized in that it produces a permanent slate of carbon dioxide, and transports it to the deep sea under pressure, or seals it in a container and dumps it into the ocean.
大気中の炭酸ガス濃度を低減させるために、炭酸ガスの
主たる排出源である化石燃料の燃焼排ガスに着目し、従
来煙突から大気中に放出していたガスの全量あるいは一
部を別系統に導き炭酸ガスのみを分離・除去し、炭酸ガ
スが除かれた排ガスは浄化ガスとして再び大気へ放出さ
せる。炭酸ガスを分離・除去する技術的手段は先ずゼオ
ライトなどの吸着剤の利用(炭酸ガスの選択的吸着およ
び脱着操作)あるいは化学吸収(2アルコキシアミンに
よる吸収)および放散操作などにより排ガス中の炭酸ガ
ス(濃度約lO%〉を90%以上の高濃度ガスとして分
離する。In order to reduce the concentration of carbon dioxide in the atmosphere, we focused on fossil fuel combustion exhaust gas, which is the main source of carbon dioxide emissions, and diverted all or part of the gas that was traditionally released into the atmosphere from chimneys to a separate system. Only carbon dioxide gas is separated and removed, and the exhaust gas from which carbon dioxide gas has been removed is released back into the atmosphere as purified gas. The technical means to separate and remove carbon dioxide gas is to first remove carbon dioxide gas from exhaust gas by using adsorbents such as zeolites (selective adsorption and desorption operations of carbon dioxide gas) or by chemical absorption (absorption by 2-alkoxyamines) and dissipation operations. (concentration about 10%) is separated as a high concentration gas of 90% or more.
本発明はこの高濃度ガスを処理することであり、このガ
スをlO℃以下の低温下で海水と混合させ、温度に対応
する圧力を加えて炭酸ガスと海水とを反応させ、固体の
水和物を生戊することである。これを分離・回収して深
海底(水深約500m)へ投入すれば深海底環境下では
この固体永和物は分解しないので再び大気中へ炭酸ガス
が放出することがなく従って燃焼排ガスから大気中へ放
出する炭酸ガスを軽減することが可能となる。The purpose of the present invention is to process this highly concentrated gas, by mixing this gas with seawater at a low temperature below 10°C, and applying pressure corresponding to the temperature to cause the carbon dioxide gas and seawater to react, thereby hydrating the solid. It is to bring something to life. If this is separated and collected and thrown into the deep seabed (approximately 500 meters deep), this solid permanent product will not decompose in the deep seabed environment, so carbon dioxide will not be released into the atmosphere again, and therefore it will be released from the combustion exhaust gas into the atmosphere. It becomes possible to reduce the amount of carbon dioxide gas released.
燃焼排ガス中の炭酸ガスを吸着・脱着などの操作により
濃縮して分離・回収する方法は既存の技術によって可能
であるがこれを海水と混合し低温加圧の条件下で反応さ
せ、炭酸ガスを水和物として固化体を作らせることが本
発明の特徴であるので、以下この原理について説明する
。It is possible to concentrate, separate and recover carbon dioxide in combustion exhaust gas through operations such as adsorption and desorption using existing technology, but it is possible to mix this with seawater and react under low temperature and pressurized conditions to release carbon dioxide. Since a feature of the present invention is to form a solidified body as a hydrate, this principle will be explained below.
炭酸ガスは水中ではガス体、液体、固体いずれの状態で
も存在するがこれは温度と圧力によって決定される。第
3図(縦軸は圧力の対数目盛、横軸温度)にCD.−L
O系の相平衡状態を示すが温度0〜lO℃の範囲におけ
る斜線部分(0℃では12.4〜3 5 atm.,
1 0℃では4 4 atm )ではCD,と8.0が
次の反応によりタラスレート水和物が生成する。Carbon dioxide exists in water as a gas, liquid, or solid, and this state is determined by temperature and pressure. Figure 3 (vertical axis is logarithmic scale of pressure, horizontal axis is temperature) shows CD. -L
The shaded area in the temperature range of 0 to 10°C shows the phase equilibrium state of the O system (12.4 to 35 atm. at 0°C,
At 10° C., 4 4 atm), CD, and 8.0, the following reaction produces talus slate hydrate.
これは水の結晶体(14面体あるいは16面体の3次元
構造の骨格)の中にCロ,分子が入り込んだ結晶構造を
もっており、しかも水に溶け難い固体化である。このタ
ラスレートは比重が約1.11であり水より重いため水
中で沈殿し、′シたがって固液分離摸作を用いて水中か
ら回収することができる。さらに深海底では温度、圧力
がタラスレートが安定する条件下にあるので深海底への
直接投入が可能でありこれが浮上することなく半永久的
に深海底へとどまることとなる。It has a crystalline structure in which carbon molecules are embedded in a water crystal (a three-dimensional framework of 14 or 16 hexahedrons), and it is a solid that is difficult to dissolve in water. This Taraslate has a specific gravity of about 1.11 and is heavier than water, so it precipitates in water and can therefore be recovered from water using a solid-liquid separation process. Furthermore, since the temperature and pressure on the deep seabed are such that the Taraslate is stable, it is possible to directly insert it into the deep seabed, where it will remain semi-permanently without surfacing.
本発明の実施例を第1図、第2図に示す。 An embodiment of the present invention is shown in FIGS. 1 and 2.
第l図は本発明のポイントとなるCOiガスのタラスレ
ート固化システムの機器構戊を示す。FIG. 1 shows the equipment structure of the COi gas slate solidification system, which is the key point of the present invention.
濃i1Cロ2ガスはコンプレッサ2で圧縮し海水と共に
タラスレート生戒槽1へ送る。タラスレート生成槽1で
は冷却器3によりCロ,ガスと水の混合物を所定温度に
冷却するが、圧力計4、温度計5を監視しながら温度と
圧力を設定する。The concentrated i1C-ro2 gas is compressed by a compressor 2 and sent to the Taraslate tank 1 together with seawater. In the Taraslate generation tank 1, a mixture of carbon gas, water, and water is cooled to a predetermined temperature by a cooler 3, and the temperature and pressure are set while monitoring a pressure gauge 4 and a thermometer 5.
次いでポンプ6により生戒タラスレートをタラスレート
分離槽7に送り固液の分離を行う。クラスレートはクラ
スレート貯槽8に保持し、タラスレート分離槽7で分離
した海水は再びタラスレート生成槽1に戻し循環使用す
る。このように一旦、固液分離して冷却海水を循環使用
することはエネルギ的に有効である。保持されたタラス
レートはコンテナ9に封入し、投棄船10で運搬し海洋
の深海底へ投入するか、あるいは圧送ボンプ1lで深海
底へ直接投入する。なお、設定する圧力、温度はクラス
レート固化体を生戊する領域であり、前述のCO2−H
20系平衡線図の斜線部分く例えば0℃では12. 4
atm以上、5℃では23atm以上、9.9℃では4
4atm以上)の範囲である。Next, the pump 6 sends the raw Taraslate to the Taraslate separation tank 7 for solid-liquid separation. The clathrate is held in a clathrate storage tank 8, and the seawater separated in the clathrate separation tank 7 is returned to the clathrate generation tank 1 for circulation use. In this way, once solid-liquid separation is performed and the cooled seawater is recycled and used, it is energy efficient. The held Taraslate is sealed in a container 9, transported by a dumping ship 10, and thrown into the deep seabed of the ocean, or directly into the deep seabed with a 1-liter pressure pump. The pressure and temperature to be set are in the range where clathrate solidification occurs, and the above-mentioned CO2-H
For example, the shaded area of the 20 series equilibrium diagram is 12. 4
atm or higher, 23 atm or higher at 5℃, 4 atm at 9.9℃
4 atm or more).
第2図は燃焼排ガスのCO,低減を目的とする本発明の
全体処理システムの流れを示すものであり、燃焼炉21
から排出するCO2ガスを含む排ガス,に対して従来、
煙突22から全量排出させていたものの全量あるいは一
部を前処理装置23に導き、ここで排ガスの温度低下、
未燃カーボンなどの除去を行ったのち、CO,分離装置
?4を経てCD2ガスだけを濃縮分離し、一方CO■ガ
スが除去されたものは浄化ガスとして大気放出する。Figure 2 shows the flow of the overall treatment system of the present invention, which aims to reduce CO in combustion exhaust gas.
Conventionally, for exhaust gas containing CO2 gas emitted from
The entire amount or a portion of the gas discharged from the chimney 22 is guided to the pretreatment device 23, where the temperature of the exhaust gas is lowered,
After removing unburned carbon etc., CO, separation equipment? 4, only the CD2 gas is concentrated and separated, while the CO2 gas from which it has been removed is released into the atmosphere as purified gas.
濃縮したCD,ガスはコンブレッサ2により圧縮し、前
述のとおり海水と混合してタラスレート生成槽1でタラ
スレート固化体を生成させる。The concentrated CD and gas are compressed by the compressor 2 and mixed with seawater as described above to produce solidified Taraslate in the Taraslate production tank 1.
これをコンテナに封入するかあるいは圧力輸送の手段に
よって深海底へ投入するようにしたものである。This is either sealed in a container or placed into the deep sea by means of pressure transport.
このように、本発明は化石燃料等燃焼排ガス中のC02
ガスの大気中へ放出する量を低減させるために排ガス中
のCO,ガスを既存技術を利用して濃度の高いCO■ガ
スとしたのち、タラスレート固化体として結晶体をつく
り、水の結晶の中にC02を強固に閉じ込めて深海底へ
投入する方法を提案するものである。In this way, the present invention can reduce CO2 in combustion exhaust gas such as fossil fuels.
In order to reduce the amount of gas released into the atmosphere, the CO gas in the exhaust gas is made into a highly concentrated CO gas using existing technology, and then a crystal body is created as a solidified Taraslate, and the CO gas is mixed into the water crystals. This project proposes a method to firmly confine CO2 and release it into the deep seabed.
本発明によれば、CO,ガスのタラスレート化は例えば
ドライアイス固化に比べて比較的温度が高く (0〜l
O℃)また加圧する圧力も45atm未満でよいため所
要動力が少なく工業的に有利な点がある。また本発明は
CO,ガスを水の結晶の中にとり込んで固化させるため
C02ガスの減容化が図れ、さらにCD2のタラスレー
ト固化を連続的に処理することが可能なシステムである
。According to the present invention, colloidal slate formation of CO and gas requires a relatively high temperature (0 to l
Furthermore, since the pressure to be applied may be less than 45 atm, the required power is small, which is industrially advantageous. In addition, the present invention is a system that can reduce the volume of CO2 gas by incorporating CO gas into water crystals and solidify it, and furthermore, can continuously process the solidification of CD2 slate.
以上の通り、Cロ2ガスを水と混合させ低温加圧操作に
よってタラスレート固化体として回収し、深海底へ投入
する本発明は大気に放出する燃焼排ガスの炭酸ガスを低
減させ、ひいては大気中の炭酸ガス濃度増加あるいは地
球の温暖化現象に対する有効な対処策である。As described above, the present invention, in which CO2 gas is mixed with water and recovered as a solidified Taraslate by low-temperature pressurization and then injected into the deep sea floor, reduces carbon dioxide gas in the combustion exhaust gas released into the atmosphere, and in turn reduces the amount of carbon dioxide in the atmosphere. This is an effective countermeasure against increasing carbon dioxide concentration or global warming.
第1図は本発明の一実施例を説明する構或図、第2図は
燃焼排ガスの処理に本発明を適用した実施例の構成図、
第3図はCD.−0.0系の相平衡状態図である。FIG. 1 is a configuration diagram illustrating an embodiment of the present invention, FIG. 2 is a configuration diagram of an embodiment in which the present invention is applied to treatment of combustion exhaust gas,
Figure 3 shows CD. It is a phase equilibrium phase diagram of -0.0 system.
Claims (1)
せる方法において、濃縮分離した炭酸ガスを海水と混合
させ低温、かつ加圧下の化学反応により水の結晶の中に
炭酸ガス分子をとり込んだクラスレート水和物を生成さ
せ、これを深海底へ圧力輸送するかあるいはコンテナに
封入して海洋投棄することを特徴とする炭酸ガスの処理
方法。A class of methods for reducing the concentration of carbon dioxide emitted into the atmosphere, such as combustion exhaust gas, in which concentrated and separated carbon dioxide is mixed with seawater and carbon dioxide molecules are incorporated into water crystals through a chemical reaction at low temperatures and under pressure. A method for processing carbon dioxide gas, which is characterized by producing a rate hydrate and transporting it under pressure to the deep seabed or sealing it in a container and dumping it into the ocean.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1300806A JPH03164419A (en) | 1989-11-21 | 1989-11-21 | Treatment of gaseous carbon dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1300806A JPH03164419A (en) | 1989-11-21 | 1989-11-21 | Treatment of gaseous carbon dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03164419A true JPH03164419A (en) | 1991-07-16 |
Family
ID=17889328
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1300806A Pending JPH03164419A (en) | 1989-11-21 | 1989-11-21 | Treatment of gaseous carbon dioxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03164419A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH03177311A (en) * | 1989-12-04 | 1991-08-01 | Mitsubishi Heavy Ind Ltd | Method for fixing carbon dioxide |
US5309672A (en) * | 1992-10-05 | 1994-05-10 | Electric Power Research Institute, Inc. | Submerged platform structure for open ocean macroalgal farm systems |
US5397553A (en) * | 1992-10-05 | 1995-03-14 | Electric Power Research Institute, Inc. | Method and apparatus for sequestering carbon dioxide in the deep ocean or aquifers |
US5700311A (en) * | 1996-04-30 | 1997-12-23 | Spencer; Dwain F. | Methods of selectively separating CO2 from a multicomponent gaseous stream |
US6106595A (en) * | 1996-04-30 | 2000-08-22 | Spencer; Dwain F. | Methods of selectively separating CO2 from a multicomponent gaseous stream |
US6352576B1 (en) | 2000-03-30 | 2002-03-05 | The Regents Of The University Of California | Methods of selectively separating CO2 from a multicomponent gaseous stream using CO2 hydrate promoters |
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