JPH04198008A - Reduction of carbon dioxide gas - Google Patents
Reduction of carbon dioxide gasInfo
- Publication number
- JPH04198008A JPH04198008A JP2331770A JP33177090A JPH04198008A JP H04198008 A JPH04198008 A JP H04198008A JP 2331770 A JP2331770 A JP 2331770A JP 33177090 A JP33177090 A JP 33177090A JP H04198008 A JPH04198008 A JP H04198008A
- Authority
- JP
- Japan
- Prior art keywords
- carbon dioxide
- dioxide gas
- catalyst
- transparent container
- trough
- 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
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims description 88
- 239000001569 carbon dioxide Substances 0.000 title claims description 44
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims description 44
- 230000009467 reduction Effects 0.000 title description 4
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000003054 catalyst Substances 0.000 claims abstract description 21
- 239000004065 semiconductor Substances 0.000 claims abstract description 10
- 229910052982 molybdenum disulfide Inorganic materials 0.000 claims abstract description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 4
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 4
- 229910052976 metal sulfide Inorganic materials 0.000 claims abstract description 4
- 229910010271 silicon carbide Inorganic materials 0.000 claims abstract description 4
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910001570 bauxite Inorganic materials 0.000 claims abstract description 3
- 239000004927 clay Substances 0.000 claims abstract description 3
- 229910052570 clay Inorganic materials 0.000 claims abstract description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 3
- 230000001678 irradiating effect Effects 0.000 claims abstract description 3
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 3
- 239000010457 zeolite Substances 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 40
- 239000001257 hydrogen Substances 0.000 claims description 17
- 229910052739 hydrogen Inorganic materials 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 13
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 13
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 13
- 239000002131 composite material Substances 0.000 claims description 3
- 229910052710 silicon Inorganic materials 0.000 claims description 3
- 239000010703 silicon Substances 0.000 claims description 3
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 3
- 229910052783 alkali metal Inorganic materials 0.000 claims description 2
- -1 alkali metal salt Chemical class 0.000 claims description 2
- 239000011521 glass Substances 0.000 abstract description 5
- 239000007795 chemical reaction product Substances 0.000 abstract description 4
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 abstract description 3
- 239000005297 pyrex Substances 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 229910052681 coesite Inorganic materials 0.000 abstract 1
- 229910052593 corundum Inorganic materials 0.000 abstract 1
- 229910052906 cristobalite Inorganic materials 0.000 abstract 1
- 229910003465 moissanite Inorganic materials 0.000 abstract 1
- 229910052961 molybdenite Inorganic materials 0.000 abstract 1
- 235000012239 silicon dioxide Nutrition 0.000 abstract 1
- 229910052682 stishovite Inorganic materials 0.000 abstract 1
- 229910052905 tridymite Inorganic materials 0.000 abstract 1
- 229910001845 yogo sapphire Inorganic materials 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 15
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 239000000047 product Substances 0.000 description 7
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 6
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 6
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 5
- 239000000446 fuel Substances 0.000 description 5
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 5
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- TVWWSIKTCILRBF-UHFFFAOYSA-N molybdenum trisulfide Chemical compound S=[Mo](=S)=S TVWWSIKTCILRBF-UHFFFAOYSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 150000003464 sulfur compounds Chemical class 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 239000004408 titanium dioxide Substances 0.000 description 3
- 238000010792 warming Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 2
- ZKKLPDLKUGTPME-UHFFFAOYSA-N diazanium;bis(sulfanylidene)molybdenum;sulfanide Chemical compound [NH4+].[NH4+].[SH-].[SH-].S=[Mo]=S ZKKLPDLKUGTPME-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002803 fossil fuel Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- WUPHOULIZUERAE-UHFFFAOYSA-N 3-(oxolan-2-yl)propanoic acid Chemical compound OC(=O)CCC1CCCO1 WUPHOULIZUERAE-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 239000005083 Zinc sulfide Substances 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 1
- 239000011609 ammonium molybdate Substances 0.000 description 1
- 229940010552 ammonium molybdate Drugs 0.000 description 1
- 235000018660 ammonium molybdate Nutrition 0.000 description 1
- UYJXRRSPUVSSMN-UHFFFAOYSA-P ammonium sulfide Chemical compound [NH4+].[NH4+].[S-2] UYJXRRSPUVSSMN-UHFFFAOYSA-P 0.000 description 1
- 229910002113 barium titanate Inorganic materials 0.000 description 1
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- CXKCTMHTOKXKQT-UHFFFAOYSA-N cadmium oxide Inorganic materials [Cd]=O CXKCTMHTOKXKQT-UHFFFAOYSA-N 0.000 description 1
- 229910052980 cadmium sulfide Inorganic materials 0.000 description 1
- CFEAAQFZALKQPA-UHFFFAOYSA-N cadmium(2+);oxygen(2-) Chemical compound [O-2].[Cd+2] CFEAAQFZALKQPA-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000010574 gas phase reaction Methods 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- YOBAEOGBNPPUQV-UHFFFAOYSA-N iron;trihydrate Chemical compound O.O.O.[Fe].[Fe] YOBAEOGBNPPUQV-UHFFFAOYSA-N 0.000 description 1
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 1
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 description 1
- 229910052808 lithium carbonate Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910000476 molybdenum oxide Inorganic materials 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 description 1
- PQQKPALAQIIWST-UHFFFAOYSA-N oxomolybdenum Chemical compound [Mo]=O PQQKPALAQIIWST-UHFFFAOYSA-N 0.000 description 1
- 238000013032 photocatalytic reaction Methods 0.000 description 1
- 238000006552 photochemical reaction Methods 0.000 description 1
- 238000001955 polymer synthesis method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 229910001930 tungsten oxide Inorganic materials 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
- 229910052984 zinc sulfide Inorganic materials 0.000 description 1
- DRDVZXDWVBGGMH-UHFFFAOYSA-N zinc;sulfide Chemical compound [S-2].[Zn+2] DRDVZXDWVBGGMH-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y02P20/121—
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
- Carbon And Carbon Compounds (AREA)
- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
a6発明の技術分野
本発明は、炭酸ガスを還元して一酸化炭素に変換し、化
成品の原料や燃料として利用するための炭酸ガスの還元
方法に関するものである。Detailed Description of the Invention a6 Technical Field of the Invention The present invention relates to a method for reducing carbon dioxide gas for reducing carbon dioxide gas and converting it into carbon monoxide for use as a raw material for chemical products or as a fuel.
b6 従来技術と問題点
近年、地球規模の環境汚染が人類の生存を脅かす問題と
して大きくクローズアップされているが、その中で最も
対策の難しい問題が炭酸ガスによる地球温暖化である。b6 Prior Art and Problems In recent years, global environmental pollution has been attracting attention as a problem that threatens the survival of humankind, but the most difficult problem to address is global warming caused by carbon dioxide gas.
炭酸ガスは、これまで問題になっできた窒素酸化物やイ
オウ酸化物などと異なり、それ自身には毒性はないが、
全世界で年間約200億トンという膨大な量が排出され
ており、大気中の炭酸ガス濃度の上昇に伴い、温室効果
による気候変動が起こり、信子万人もの環境難民が発生
すると危ぐされている。これを防止するため、エネルギ
ー代替や省エネルギーなどによる炭酸ガス排出の抑制が
政策的に推進されようとしているが、炭酸ガスの排出は
経済社会の発展と密接な関係を持っているため、その大
幅な抑制は極めて難しい情勢である。したがって、炭酸
ガスによる地球温暖化を阻止するためには炭酸ガスの還
元・固定化技術の開発が不可欠である。炭酸ガスを水素
と反応させて還元する接触水素化反応による炭酸ガスの
還元・固定化法は、光化学反応法や電気化学反応法、高
分子合成による方法、有機合成による方法などと比べ、
単位時間、単位面積当りの炭酸ガスの還元・固定化能力
が大きく、大量の炭酸ガスの処理が可能である。また、
既存のフィッシャー・トロプシュ法炭化水素合成技術な
どが応用でき、気相反応であるため、生成物の分離が容
易などの利点も持っている。これまで接触水素化反応に
よる炭酸ガスの還元・固定化法として、ルテニウムやロ
ジウムなどの貴金属触媒を用いる方法が研究されてきた
(例えば、F、 Solymosi and A。Carbon dioxide gas is not toxic in itself, unlike nitrogen oxides and sulfur oxides, which have caused problems in the past.
A huge amount of carbon dioxide, approximately 20 billion tons, is emitted worldwide every year, and as the concentration of carbon dioxide increases in the atmosphere, climate change due to the greenhouse effect will occur, and it is feared that as many as Nobuko will become environmental refugees. . To prevent this, policies are trying to promote the reduction of carbon dioxide emissions through energy substitution and energy conservation, but since carbon dioxide emissions are closely related to economic and social development, This is an extremely difficult situation to suppress. Therefore, in order to prevent global warming caused by carbon dioxide gas, it is essential to develop technologies for reducing and fixing carbon dioxide gas. The method of reducing and fixing carbon dioxide by catalytic hydrogenation reaction, in which carbon dioxide is reacted with hydrogen and reduced, is more effective than photochemical reaction method, electrochemical reaction method, polymer synthesis method, organic synthesis method, etc.
It has a large capacity to reduce and fix carbon dioxide per unit time and unit area, and can process large amounts of carbon dioxide. Also,
Existing Fischer-Tropsch hydrocarbon synthesis technology can be applied to this process, and since it is a gas phase reaction, it has the advantage of easy product separation. Until now, methods using noble metal catalysts such as ruthenium and rhodium have been studied as a method for reducing and fixing carbon dioxide gas by catalytic hydrogenation reaction (for example, F, Solymosi and A.
Erdohelyi 、 J、 Mo1.Catal、
、 8.471 (1980))。Erdohelyi, J., Mo1. Catal,
, 8.471 (1980)).
しかしこの方法は、l)使用する触媒が高価であり、硫
化水素や亜硫酸ガスなどのイオウ化合物によって簡単に
被毒され、触媒活性が急激に低下する、2)この反応で
は炭酸ガスがメタンに還元されるが、この反応は原料よ
りも生成物の自由エネルギーが低い発エルゴン反応であ
るため、エネルギー歩留まりが悪い、3)一般に反応温
度が350℃〜500℃と高く、その温度を発生するた
めに化石燃料を使用するため、実質的に炭酸ガスの排出
抑制にさえもならない、などの欠点を持っていた。However, this method has two drawbacks: (1) the catalyst used is expensive and is easily poisoned by sulfur compounds such as hydrogen sulfide and sulfur dioxide gas, resulting in a rapid decrease in catalytic activity; (2) in this reaction, carbon dioxide gas is reduced to methane; However, this reaction is an exergonic reaction in which the free energy of the product is lower than that of the raw material, so the energy yield is poor.3) The reaction temperature is generally high at 350°C to 500°C, and it is Since it uses fossil fuels, it has the disadvantage that it does not even substantially reduce carbon dioxide emissions.
C0発明の目的
本発明は上記の点に鑑み、炭酸ガスによる地球温暖化に
対処して、化石燃料を使用せず、炭酸ガスを排出しない
無公害の太陽エネルギーを利用した、イオウ化合物によ
って被毒されずに耐久性があり、経済的でエネルギー歩
留まりの良い、炭酸ガスの一酸化炭素への還元方法の提
供を目的とするものである。C0 Purpose of the Invention In view of the above, the present invention addresses global warming caused by carbon dioxide gas, and uses non-polluting solar energy that does not use fossil fuels or emit carbon dioxide. The purpose of the present invention is to provide a method for reducing carbon dioxide gas to carbon monoxide, which is durable, economical, and has a high energy yield.
d0発明の構成
この目的は本発明によれば、太陽集光集熱器の焦点付近
に硫化モリブデン触媒を充填した透明容器を設置し、集
光した太陽光を照射しながら、炭酸ガスと水素を含んだ
ガスを流通させることによって達成される。炭酸ガスは
硫化モリブデン触媒上で水素と反応し一酸化炭素に変換
されるが、一酸化炭素はそのまま燃料としても使用でき
るし、既存の合成ガス(一酸化炭素と水素)からのメタ
ノール製造プロセスやC1化学技術などを利用して、最
近、自動車用燃料として脚光を浴びているメタノールや
化成品の原料に変換して利用することもできる。この炭
酸ガスを一酸化炭素に変換する反応は吸エルゴン反応で
あるため、エネルギー歩留まりが良く、生成物である一
酸化炭素は太陽エネルギーを蓄えたことになる。本発明
に用いられる硫化モリブデン触媒としては、二硫化モリ
ブデンや三硫化モリブデンの他に低級及び高級硫化物を
含んだものや、さらにそれに酸化モリブデンを含んだも
のなどが挙げられるが、特に多孔質で表面積の大きな二
硫化モリブデンあるいは二硫化モリブデンをアルミナや
シリカ、活性炭、ゼオライト、活性白土、ボーキサイト
、ケイ素、炭化ケイ素、金属酸化物半導体、金属硫化物
半導体などの担体に担持したものが好ましい。これらの
担体も多孔質や微粒子などの表面積の大きなものが好ま
しい。二硫化モリブデンは譚水鉛鉱として地殻中に広く
分布し、潤滑剤などとして市販されており、安価で低毒
性の物質であり、黒色で太陽光の吸収率が大きく、硫化
水素や亜硫酸ガスなどのイオウ化合物によって被毒され
ず、逆に触媒性能が向上するという特長を持っている。d0 Structure of the Invention According to the present invention, a transparent container filled with a molybdenum sulfide catalyst is installed near the focal point of a solar collector, and carbon dioxide and hydrogen are generated while irradiating the concentrated sunlight. This is achieved by circulating a gas containing it. Carbon dioxide reacts with hydrogen on a molybdenum sulfide catalyst and is converted to carbon monoxide, but carbon monoxide can be used as fuel as is, and it can also be used in the existing methanol production process from synthesis gas (carbon monoxide and hydrogen). Using C1 chemical technology, it can also be used by converting it into methanol, which has recently been in the spotlight as an automobile fuel, and into raw materials for chemical products. Since the reaction that converts carbon dioxide gas into carbon monoxide is an endergonic reaction, the energy yield is high, and the carbon monoxide product stores solar energy. Examples of the molybdenum sulfide catalyst used in the present invention include those containing lower and higher sulfides in addition to molybdenum disulfide and molybdenum trisulfide, and those containing molybdenum oxide. Preferably, molybdenum disulfide or molybdenum disulfide having a large surface area is supported on a carrier such as alumina, silica, activated carbon, zeolite, activated clay, bauxite, silicon, silicon carbide, metal oxide semiconductor, metal sulfide semiconductor, or the like. These carriers are preferably porous or have a large surface area, such as fine particles. Molybdenum disulfide is widely distributed in the earth's crust as hydrite, and is commercially available as a lubricant. It is an inexpensive and low-toxic substance, is black in color, has a high absorption rate of sunlight, and is highly effective against hydrogen sulfide and sulfur dioxide gas. It has the feature that it is not poisoned by sulfur compounds and, on the contrary, improves catalytic performance.
多孔質の二硫化モリブデンはモリブデン酸アンモニウム
の水溶液に硫化水素や硫化アンモニウムを飽和させるな
どして得られるテトラチオモリブデン酸アンモニウムを
希硫酸や硝酸によって分解したり、窒素気流中や水素気
流中で加熱することによって得られる。また、三硫化モ
リブデンを熱分解したり、三硫化モリブデンを硫化水素
気流中で加熱することなどによっても得られる。担持硫
化モリブデン触媒は、テトラチオモリブデン酸アンモニ
ウムの水溶液あるいはアンモニア水溶液に担体を攪はん
しながら加え、乾燥した後、水素気流中などで加熱分解
するなどの方法で調製される。担体に、ケイ素や炭化ケ
イ素、硫化亜鉛や硫化カドミウムなどの金属硫化物半導
体、酸化亜鉛や酸化タングステン、酸化カドミウム、二
酸化チタン、三二酸化鉄、チタン酸バリウムなどの金属
酸化物半導体のような半導体を用いた場合には、担体で
ある半導体が光の照射によって光触媒反応を起こすため
、炭酸ガスの還元が促進される。本発明に用いられる太
陽集光集熱器は田型平面鏡集光集熱器や樋型複合放物面
鏡集光集熱器、樋型放物面鏡集光集熱器、樋型放物面航
を平面鏡で疑似した集光集熱器、回転放物面鏡集光集熱
器、線型フレネルレンズ集光集熱器、円型フレネルレン
ズ集光集熱器などの集光型太陽集熱器が挙げられる1本
発明に用いられる透明容器の材質はガスを透過したり、
ガスと反応したすせず、透明で200. 300℃程度
の耐熱性を持つものであれば、ガラスやプラスチックな
ど、どのような材質でも良いが、特に石英やバイコール
ガラス、パイレックスガラスなどの短波長の光でも透過
するものが好ましい。また、透明容器の形状は太陽集光
集熱器として回転放物面鏡集光集熱器や円型フレネルレ
ンズ集光集熱器などの点集光型集熱器を用いる場合には
円盤状や球状、角柱状などの容器が用いられ、線型フレ
ネルレンズ集光集熱器や田型の集光集熱器などの線集光
型集熱器を用いる場合には直管状などの容器が用いられ
る。この際、円盤状容器の側面や底面をミラーにしたり
、断熱材を施したりしたものや、直管状容器を二重管に
し、外管に選択吸収膜をコーティングしたり、内管と外
管の間を真空にしたものを使用することによって、放熱
を抑制し、反応を促進させることができる。本発明で透
明容器に流通させるガスは炭酸ガスと水素を含んだガス
で、アルゴンやヘリウムなどの不活性ガス、メタンなど
の炭化水素、一酸化炭素やアルコール、硫化水素などを
含んでいても良い。炭酸ガスと水素の割合は1対1ある
いは水素の方が過剰のものが好ましい。Porous molybdenum disulfide is obtained by saturating an aqueous solution of ammonium molybdate with hydrogen sulfide or ammonium sulfide, decomposing ammonium tetrathiomolybdate with dilute sulfuric acid or nitric acid, or heating it in a nitrogen or hydrogen stream. obtained by doing. It can also be obtained by thermally decomposing molybdenum trisulfide or heating molybdenum trisulfide in a hydrogen sulfide stream. The supported molybdenum sulfide catalyst is prepared by adding a carrier to an aqueous solution of ammonium tetrathiomolybdate or aqueous ammonia with stirring, drying, and then thermally decomposing it in a hydrogen stream. Semiconductors such as silicon, silicon carbide, metal sulfide semiconductors such as zinc sulfide and cadmium sulfide, and metal oxide semiconductors such as zinc oxide, tungsten oxide, cadmium oxide, titanium dioxide, iron sesquioxide, and barium titanate are used as carriers. When used, the semiconductor carrier undergoes a photocatalytic reaction upon irradiation with light, promoting the reduction of carbon dioxide gas. The solar collectors used in the present invention are a field-shaped flat mirror collector, a trough-type composite parabolic mirror collector, a trough-type parabolic mirror collector, and a trough-type parabolic collector. Concentrating solar heat collectors such as a concentrator that simulates a surface beam using a plane mirror, a rotating parabolic mirror concentrator, a linear Fresnel lens concentrator, and a circular Fresnel lens concentrator. The transparent container used in the present invention is made of a material that is permeable to gas,
No soot reacts with gas, transparent and 200. Any material such as glass or plastic may be used as long as it has heat resistance of about 300°C, but materials that can transmit even short wavelength light such as quartz, Vycor glass, and Pyrex glass are particularly preferred. In addition, the shape of the transparent container is disk-shaped when using a point-concentrating solar collector such as a rotating parabolic mirror collector or a circular Fresnel lens collector. Containers such as spherical, prismatic, etc. are used, and when using linear concentrators such as linear Fresnel lens concentrators and field-shaped concentrators, containers such as straight tubes are used. It will be done. In this case, the sides and bottom of the disc-shaped container may be mirrored or insulated, the straight tubular container may be made into a double pipe, the outer pipe may be coated with a selective absorption membrane, or the inner and outer pipes may be coated with a selective absorption membrane. By using a vacuum chamber, heat radiation can be suppressed and the reaction can be accelerated. The gas flowing through the transparent container in the present invention is a gas containing carbon dioxide and hydrogen, and may also contain inert gases such as argon and helium, hydrocarbons such as methane, carbon monoxide, alcohol, hydrogen sulfide, etc. . The ratio of carbon dioxide gas to hydrogen is preferably 1:1 or an excess of hydrogen.
これらのガスを透明容器に連続的に流通させても良いし
、断続的に流通させても良い。そのとき、触媒が容器か
ら流出しないようにグラスウールなどで容器の入口と出
口に栓をすることが望ましい。These gases may be passed through the transparent container continuously or intermittently. At this time, it is desirable to plug the inlet and outlet of the container with glass wool or the like to prevent the catalyst from flowing out of the container.
透明容器に硫化モリブデン触媒を充填し、炭酸ガスと水
素を含んだガスを流通させながら、集光した太陽光を照
射して炭酸ガスを還元する場合、この反応は吸エルゴン
反応であり、反応温度が高い方が反応率が大きいため1
反応ガスや透明容器を工場廃熱などで加熱しても良い。When a transparent container is filled with a molybdenum sulfide catalyst and gas containing carbon dioxide and hydrogen is passed through it, carbon dioxide is reduced by irradiation with concentrated sunlight.This reaction is an endergonic reaction, and the reaction temperature Since the higher the reaction rate is, 1
The reaction gas and transparent container may be heated using factory waste heat.
また、低温での反応率を上げるため、アルカリ金属塩、
特に炭酸ナトリウムや炭酸リチウムを添加した硫化モリ
ブデン触媒を用いても良い。In addition, to increase the reaction rate at low temperatures, alkali metal salts,
In particular, a molybdenum sulfide catalyst to which sodium carbonate or lithium carbonate is added may be used.
e4発明の実施例
以下、本発明の代表的な実施例を図面によって説明する
。e4 Embodiments of the invention Hereinafter, typical embodiments of the invention will be described with reference to the drawings.
第1図は本発明の一実施例で、円型フレネルレンズ集光
集熱器を用いたものである。直径1.5mのフレネルレ
ンズ1の焦点付近に直径5cmのパイレックスガラス製
の円盤状透明容器2を設置し、その中に3gの二酸化チ
タンに担持した硫化モリブデン触媒3を充填し、炭酸ガ
スと水素の1−=1の混合ガス4を6ml/minの流
量で流通させながら、集光した太陽光を照射し、得られ
た反応生成物5をガスクロマトグラフを用いて分析した
。その結果、約10%の炭酸ガスが一酸化炭素に変換さ
れていた。FIG. 1 shows an embodiment of the present invention, which uses a circular Fresnel lens condenser. A disc-shaped transparent container 2 made of Pyrex glass with a diameter of 5 cm is installed near the focal point of a Fresnel lens 1 with a diameter of 1.5 m, and a molybdenum sulfide catalyst 3 supported on 3 g of titanium dioxide is filled in the container, and carbon dioxide gas and hydrogen While flowing a mixed gas 4 of 1-=1 at a flow rate of 6 ml/min, concentrated sunlight was irradiated, and the resulting reaction product 5 was analyzed using a gas chromatograph. As a result, approximately 10% of carbon dioxide gas was converted to carbon monoxide.
第2図は本発明の他の実施例を示したもので、追尾機構
を用いないで集光集熱できる樋型複合放物面鏡集光集熱
器を用いたものである。内部にミラー6を施した長さ5
0cmの集光集熱器7の焦点付近に、直径1cmの石英
でできた直管状透明容器8を設置し、その内部に15g
の触媒9(二酸化チタンに担持した二硫化モリブデンに
炭酸ナトリウムを添加したもの)を充填し、炭酸ガスと
水素とアルゴンの11: 1の混合ガス10を6ml
/minの流量で流通しながら、集光した太陽光を照射
し、得られた反応生成物11をガスクロマトグラフを用
いて分析した。その結果、約12%の炭酸ガスが一酸化
炭素に変換されていた6f1発明の効果
本発明は以上説明したように、太陽集光集熱器によって
集光した太陽光を用いて、透明容器内に充填した硫化モ
リブデン上で炭酸ガスを水素と反応させて一酸化炭素に
変換するもので、黒色で太陽光の吸取率がよく、低温で
しかも常圧で反応を起こすことができる安価で低毒性で
イオウ化合物によって被毒されない硫化モリブデン触媒
を用いることによって、これまで反応温度が高かったた
め難しかった太陽エネルギーによる炭酸ガスの直接的還
元を可能にしたものである。この反応は吸エルゴン反応
であるためエネルギーの歩留まりが良く、生成物である
一酸化炭素はそのまま燃料としても利用できるし、自動
車用燃料として脚光を浴びているメタノールや化成品の
原料に変換して利用することもできるため、地球環境保
全の面からもエネルギ一対策の面からも非常に有効であ
る。FIG. 2 shows another embodiment of the present invention, which uses a trough-type composite parabolic mirror light collector that can collect light and heat without using a tracking mechanism. Length 5 with mirror 6 inside
A straight tubular transparent container 8 made of quartz with a diameter of 1 cm is installed near the focal point of the 0 cm condensing collector 7, and 15 g of water is placed inside it.
of catalyst 9 (sodium carbonate added to molybdenum disulfide supported on titanium dioxide) and 6 ml of mixed gas 10 of 11:1 of carbon dioxide, hydrogen, and argon.
While flowing at a flow rate of /min, concentrated sunlight was irradiated, and the obtained reaction product 11 was analyzed using a gas chromatograph. As a result, about 12% of carbon dioxide gas was converted to carbon monoxide.Effects of the 6f1 Invention As explained above, the present invention uses sunlight collected by a solar collector to create a It converts carbon dioxide gas into carbon monoxide by reacting it with hydrogen on molybdenum sulfide filled in the tank.It is black in color, has a good sunlight absorption rate, and is inexpensive and low-toxic because it can react at low temperatures and at normal pressure. By using a molybdenum sulfide catalyst that is not poisoned by sulfur compounds, it has become possible to directly reduce carbon dioxide gas using solar energy, which was previously difficult due to the high reaction temperature. Since this reaction is an endergonic reaction, the yield of energy is high, and the product carbon monoxide can be used as fuel as it is, or it can be converted into methanol, which is in the spotlight as an automobile fuel, and raw materials for chemical products. Because it can be used for various purposes, it is very effective from the perspective of global environmental conservation and energy conservation.
m1図m2図は本発明の炭酸ガス還元方法の実施例を示
す模式図である。
図中符号1はフレネルレンズ、2は透明容器、3は触媒
、4は炭酸ガスと水素の混合ガス、5は反応生成物、6
はミラー、7は集光集熱器、8は炭酸ガスと水素とアル
ゴンの混合ガス。
富山朔太部Figures m1 and m2 are schematic diagrams showing examples of the carbon dioxide reduction method of the present invention. In the figure, 1 is a Fresnel lens, 2 is a transparent container, 3 is a catalyst, 4 is a mixed gas of carbon dioxide and hydrogen, 5 is a reaction product, 6
is a mirror, 7 is a condenser, and 8 is a mixed gas of carbon dioxide, hydrogen, and argon. Toyama Sakuta
Claims (4)
充填した透明容器を設置し、その中に炭酸ガスと水素を
含んだガスを流通させながら、集光した太陽光を透明容
器内の触媒に照射し、触媒上で炭酸ガスを水素と反応さ
せて、一酸化炭素に変換することを特徴とする炭酸ガス
の還元方法。1. A transparent container filled with molybdenum sulfide catalyst is installed near the focal point of the solar collector, and while gas containing carbon dioxide and hydrogen is flowing through the container, the concentrated sunlight is applied to the catalyst inside the transparent container. A method for reducing carbon dioxide gas, which is characterized by irradiating the carbon dioxide gas, reacting it with hydrogen on a catalyst, and converting it into carbon monoxide.
形複合放物面鏡集光集熱器、樋型放物面鏡集光集熱器、
樋形放物面鏡を平面鏡で疑似した集光集熱器、回転放物
面鏡集光集熱器、線型フレネルレンズ集光集熱器、円型
フレネルレンズ集光集熱器などの集光型太陽集熱器を用
いることを特徴とする特許請求の範囲第1項記載の炭酸
ガス還元方法。2. As solar collectors, we use trough-shaped flat mirror collectors, trough-shaped composite parabolic mirror collectors, trough-shaped parabolic mirror collectors,
Light concentrators that simulate a trough-shaped parabolic mirror with a plane mirror, rotating parabolic mirror concentrators, linear Fresnel lens concentrators, circular Fresnel lens concentrators, etc. The method for reducing carbon dioxide gas according to claim 1, characterized in that a type solar collector is used.
性炭、ゼオライト、活性白土、ボーキサイト、ケイ素、
炭化ケイ素、金属酸化物半導体、金属硫化物半導体のう
ちの少なくとも1種類の担体に担持した二硫化モリブデ
ンを用いることを特徴とする特許請求の範囲第1項記載
の炭酸ガス還元方法。3. Molybdenum sulfide catalysts include alumina, silica, activated carbon, zeolite, activated clay, bauxite, silicon,
The method for reducing carbon dioxide gas according to claim 1, characterized in that molybdenum disulfide supported on at least one type of carrier selected from silicon carbide, a metal oxide semiconductor, and a metal sulfide semiconductor is used.
した担持二硫化モリブデンを用いることを特徴とする特
許請求の範囲第1項記載の炭酸ガス還元方法。4. The method for reducing carbon dioxide gas according to claim 1, characterized in that supported molybdenum disulfide to which an alkali metal salt is added is used as the molybdenum sulfide catalyst.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2331770A JPH0723207B2 (en) | 1990-11-29 | 1990-11-29 | Carbon dioxide reduction method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2331770A JPH0723207B2 (en) | 1990-11-29 | 1990-11-29 | Carbon dioxide reduction method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04198008A true JPH04198008A (en) | 1992-07-17 |
| JPH0723207B2 JPH0723207B2 (en) | 1995-03-15 |
Family
ID=18247430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2331770A Expired - Lifetime JPH0723207B2 (en) | 1990-11-29 | 1990-11-29 | Carbon dioxide reduction method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0723207B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116239435A (en) * | 2023-03-17 | 2023-06-09 | 华东师范大学 | A method for constructing a catalyst-free 185nm photochemical reaction system and its application |
| CN120605741A (en) * | 2025-08-12 | 2025-09-09 | 宁波大学 | A KOH-loaded molybdenum disulfide photothermal catalyst and its preparation method and application |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5551712A (en) * | 1978-10-13 | 1980-04-15 | Agency Of Ind Science & Technol | Production of carbon monoxide from carbon dioxide using sulfur |
| JPS6380833A (en) * | 1986-09-25 | 1988-04-11 | Toyota Central Res & Dev Lab Inc | Method and device for purifying vehicle interior odor |
-
1990
- 1990-11-29 JP JP2331770A patent/JPH0723207B2/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5551712A (en) * | 1978-10-13 | 1980-04-15 | Agency Of Ind Science & Technol | Production of carbon monoxide from carbon dioxide using sulfur |
| JPS6380833A (en) * | 1986-09-25 | 1988-04-11 | Toyota Central Res & Dev Lab Inc | Method and device for purifying vehicle interior odor |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116239435A (en) * | 2023-03-17 | 2023-06-09 | 华东师范大学 | A method for constructing a catalyst-free 185nm photochemical reaction system and its application |
| CN120605741A (en) * | 2025-08-12 | 2025-09-09 | 宁波大学 | A KOH-loaded molybdenum disulfide photothermal catalyst and its preparation method and application |
| CN120605741B (en) * | 2025-08-12 | 2025-12-05 | 宁波大学 | A KOH-supported molybdenum disulfide photothermal catalyst, its preparation method and application |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0723207B2 (en) | 1995-03-15 |
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