JPH0723207B2 - Carbon dioxide reduction method - Google Patents
Carbon dioxide reduction methodInfo
- Publication number
- JPH0723207B2 JPH0723207B2 JP2331770A JP33177090A JPH0723207B2 JP H0723207 B2 JPH0723207 B2 JP H0723207B2 JP 2331770 A JP2331770 A JP 2331770A JP 33177090 A JP33177090 A JP 33177090A JP H0723207 B2 JPH0723207 B2 JP H0723207B2
- Authority
- JP
- Japan
- Prior art keywords
- carbon dioxide
- concentrator
- catalyst
- gutter
- hydrogen
- 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 - Lifetime
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
- 238000000034 method Methods 0.000 title claims description 17
- 230000009467 reduction Effects 0.000 title claims description 8
- 239000007789 gas Substances 0.000 claims description 29
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 claims description 21
- 239000003054 catalyst Substances 0.000 claims description 18
- 239000001257 hydrogen Substances 0.000 claims description 18
- 229910052739 hydrogen Inorganic materials 0.000 claims description 18
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 16
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 13
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 12
- 229910052982 molybdenum disulfide Inorganic materials 0.000 claims description 8
- 239000004065 semiconductor Substances 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 230000001678 irradiating effect Effects 0.000 claims description 3
- 229910044991 metal oxide Inorganic materials 0.000 claims description 3
- 150000004706 metal oxides Chemical class 0.000 claims description 3
- 229910052976 metal sulfide Inorganic materials 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
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 3
- 229910021536 Zeolite Inorganic materials 0.000 claims description 2
- 229910052783 alkali metal Inorganic materials 0.000 claims description 2
- -1 alkali metal salt Chemical class 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 2
- 229910001570 bauxite Inorganic materials 0.000 claims description 2
- 239000004927 clay Substances 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 claims description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 239000010457 zeolite Substances 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 description 15
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- 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
- 238000010521 absorption reaction Methods 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 239000000446 fuel Substances 0.000 description 5
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 4
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 229910000037 hydrogen sulfide Inorganic materials 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
- UEUXEKPTXMALOB-UHFFFAOYSA-J tetrasodium;2-[2-[bis(carboxylatomethyl)amino]ethyl-(carboxylatomethyl)amino]acetate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]C(=O)CN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O UEUXEKPTXMALOB-UHFFFAOYSA-J 0.000 description 4
- 229910052786 argon Inorganic materials 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000007795 chemical reaction product Substances 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
- 239000004408 titanium dioxide Substances 0.000 description 3
- 238000010792 warming Methods 0.000 description 3
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-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
- 239000000969 carrier Substances 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
- 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
- 150000002431 hydrogen Chemical class 0.000 description 2
- 239000005297 pyrex Substances 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- 229910000029 sodium carbonate Inorganic materials 0.000 description 2
- 230000001629 suppression Effects 0.000 description 2
- 238000003786 synthesis reaction Methods 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
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonium chloride Substances [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 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
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-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
- 235000011114 ammonium hydroxide Nutrition 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
- JRPBQTZRNDNNOP-UHFFFAOYSA-N barium titanate Chemical compound [Ba+2].[Ba+2].[O-][Ti]([O-])([O-])[O-] JRPBQTZRNDNNOP-UHFFFAOYSA-N 0.000 description 1
- 229910002113 barium titanate Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015572 biosynthetic process 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
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000009903 catalytic hydrogenation reaction Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 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
- 230000017525 heat dissipation Effects 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
- 230000003100 immobilizing effect Effects 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 150000008040 ionic compounds Chemical class 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
- 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
- 231100000053 low toxicity Toxicity 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052961 molybdenite Inorganic materials 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
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 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
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000001955 polymer synthesis method Methods 0.000 description 1
- 230000008569 process 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
- 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
- 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)
Description
【発明の詳細な説明】 a.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。Description: TECHNICAL FIELD OF THE INVENTION The present invention relates to a carbon dioxide reduction method for reducing carbon dioxide to convert it into carbon monoxide and using it as a raw material or fuel for chemical products. .
b.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。
炭酸ガスは、これまで問題になって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、何千万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.Erdohelyi,J.Mol.Catal.,8,47
1(1980))。しかしこの方法は、1)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ン化合物
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。b. Conventional technology and problems In recent years, global environmental pollution has been widely highlighted as a problem that threatens the survival of humankind, but the most difficult problem to address is global warming due to carbon dioxide.
Carbon dioxide is not toxic by itself, unlike nitrogen oxides and sulfur oxides, which have been problematic so far,
The world emits a huge amount of about 20 billion tons per year, and with the increase of carbon dioxide concentration in the atmosphere, climate change due to the greenhouse effect will occur, and it is threatened that tens of millions of environmental refugees will occur. There is. In order to prevent this, the suppression of carbon dioxide emissions through energy substitution and energy saving is being promoted as a policy, but since carbon dioxide emissions are closely related to economic and social development, the Suppression is an extremely difficult situation. Therefore, in order to prevent the global warming caused by carbon dioxide, the development of carbon dioxide reduction / immobilization technology is indispensable. Compared with photochemical reaction method, electrochemical reaction method, polymer synthesis method, organic synthesis method, etc., carbon dioxide gas reduction / immobilization method by catalytic hydrogenation reaction that reacts carbon dioxide gas with hydrogen The ability to reduce and immobilize carbon dioxide per unit area is large, and a large amount of carbon dioxide can be treated. In addition, existing Fischer-Tropsch hydrocarbon synthesis technology can be applied, and since it is a gas phase reaction, it also has the advantage of easy separation of products. As a method for reducing and immobilizing carbon dioxide by catalytic hydrogen reaction, a method using a noble metal catalyst such as ruthenium or rhodium has been studied so far (for example, F. Solymosi and A. Erdohelyi, J. Mol. Catal., 8 , 47
1 (1980)). However, in this method, 1) the catalyst used is expensive, and it is easily poisoned by ionic compounds such as hydrogen sulfide and sulfurous acid gas, and the catalytic activity sharply decreases.
2) In this reaction, carbon dioxide is reduced to methane, but this reaction is an ergon reaction with a lower free energy of the product than the raw material, so the energy yield is poor.
3) Generally, the reaction temperature is as high as 350 ° C. to 500 ° C., and since fossil fuel is used to generate that temperature, it has a drawback that it does not substantially suppress the emission of carbon dioxide gas.
c.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。c. Object of the invention In view of the above points, the present invention addresses the global warming caused by carbon dioxide gas, and uses sulfur compounds, which use pollution-free solar energy that does not use fossil fuels and emits no carbon dioxide gas. It is an object of the present invention to provide a method of reducing carbon dioxide gas to carbon monoxide, which is durable without poisoning, is economical, and has a high energy yield.
d.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輝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。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。本発明に用いる
太陽集光集熱器は樋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
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が挙げられる。
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、ガスと反応したりせず、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樋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イングしたり、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。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。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、反応ガスや透明容器を工場廃熱などで加熱し
ても良い。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。d. 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 the solar concentrator, and while irradiating the concentrated sunlight, carbon dioxide and hydrogen are emitted. It is achieved by circulating a gas containing Carbon dioxide gas is converted to carbon monoxide by reacting with hydrogen on a molybdenum sulfide catalyst, but carbon monoxide can be used as it is as a fuel, as well as in the process for producing methanol from existing syngas (carbon monoxide and hydrogen). It can also be used by converting it to a raw material for methanol and chemical products, which have recently been spotlighted as fuel for automobiles, using C1 chemical technology. Since the reaction of converting carbon dioxide gas into carbon monoxide is an absorption ergon reaction, the energy yield is good, and the product carbon monoxide has stored solar energy. Examples of molybdenum sulfide catalysts 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, and the like, but are particularly porous. It is preferable to support molybdenum disulfide or molybdenum disulfide having a large surface area on a carrier such as alumina, silica, activated carbon, zeolite, activated clay, bauxite, silicon, silicon carbide, metal oxide semiconductor, metal sulfide semiconductor. It is preferable that these carriers also have a large surface area such as porous and fine particles. Molybdenum disulfide, which is widely distributed in the crust as molybdenite and is commercially available as a lubricant, is an inexpensive and low-toxic substance that is black and has a high absorption rate for sunlight. It has the feature that it is not poisoned by sulfur compounds and, on the contrary, the catalytic performance is improved. Porous molybdenum disulfide is obtained by saturating hydrogen sulfide or ammonium sulfide in an aqueous solution of ammonium molybdate to decompose ammonium tetrathiomolybdate with dilute sulfuric acid or nitric acid, or heating it in a nitrogen stream or hydrogen stream. It is obtained by doing. It can also be obtained by thermally decomposing molybdenum trisulfide, or heating molybdenum trisulfide in a hydrogen sulfide gas stream. The supported molybdenum sulfide catalyst is prepared by a method in which a carrier is added to an aqueous solution of ammonium tetrathiomolybdate or an aqueous ammonia solution with stirring, dried, and then thermally decomposed in a hydrogen stream or the like. As carriers, semiconductors such as metal sulfide semiconductors such as silicon and silicon carbide, zinc sulfide and cadmium sulfide, and metal oxide semiconductors such as zinc oxide and tungsten oxide, cadmium oxide, titanium dioxide, iron sesquioxide, and barium titanate. If used,
The semiconductor, which is a carrier, causes a photocatalytic reaction by irradiation with light, so that the reduction of carbon dioxide is promoted. The solar concentrator used in the present invention is a gutter type flat mirror concentrator, a gutter type composite parabolic concentrator, a gutter type parabolic concentrator, a gutter type parabolic collector. Concentrating solar collectors such as collectors that simulate mirrors with plane mirrors, rotating parabolic mirror collectors, linear Fresnel lens collectors, and circular Fresnel lens collectors. Is mentioned.
The material of the transparent container used in the present invention is permeable to gas, does not react with gas, is transparent and has heat resistance of about 200,300 ° C., glass, plastic, etc.,
Although any material may be used, a material such as quartz, Vycor glass, or Pyrex glass that transmits short wavelength light is particularly preferable. The shape of the transparent container is disc-shaped when using a point concentrator such as a rotating parabolic concentrator or a circular Fresnel lens concentrator as the solar concentrator. , Spherical, prismatic, etc. are used, and when using a linear light collector such as a linear Fresnel lens collector or gutter collector, a straight container is used. To be
At this time, the side or bottom of the disk-shaped container is used as a mirror, or a heat-insulating material is applied, or a straight tubular container is made into a double pipe,
By coating the outer tube with a selective absorption film or using a vacuum between the inner tube and the outer tube, heat dissipation can be suppressed and the reaction can be promoted. In the present invention, the gas passed through the transparent container is a gas containing carbon dioxide and hydrogen,
It may contain an inert gas such as argon or helium, a hydrocarbon such as methane, carbon monoxide, alcohol, hydrogen sulfide, or the like. The ratio of carbon dioxide gas to hydrogen is preferably 1: 1 or hydrogen is in excess. These gases may be continuously circulated in the transparent container or may be intermittently circulated. At that time, it is desirable to plug the inlet and outlet of the container with glass wool or the like so that the catalyst does not flow out of the container. When a transparent container is filled with a molybdenum sulfide catalyst and a carbon dioxide gas and a gas containing hydrogen are circulated while the concentrated sunlight is irradiated to reduce the carbon dioxide gas, this reaction is an absorption ergon reaction. Since the higher the ratio, the higher the reaction rate, the reaction gas or the transparent container may be heated with factory waste heat. Further, in order to increase the reaction rate at low temperature, a molybdenum sulfide catalyst added with an alkali metal salt, particularly sodium carbonate or lithium carbonate, may be used.
e.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。e. Embodiments of the Invention Hereinafter, representative embodiments of the present 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 in which a circular Fresnel lens condenser collector is used. A disk-shaped transparent container 2 made of Pyrex glass having a diameter of 5 cm is installed near the focal point of a Fresnel lens 1 having a diameter of 1.5 m, and a molybdenum sulfide catalyst 3 supported on 3 g of titanium dioxide is filled in the transparent container 2 of carbon dioxide and hydrogen. While flowing 1: 1 mixed gas 4 at a flow rate of 6 ml / min,
The condensed sunlight was irradiated and the obtained reaction product 5 was analyzed using a gas chromatograph. As a result, about 10% of carbon dioxide was converted into 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50
cmの集光集熱器7の集点付近に、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1:1:1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。FIG. 2 shows another embodiment of the present invention, which uses a gutter-type compound parabolic mirror collector that can collect and collect heat without using a tracking mechanism. Length 50 with mirror 6 inside
A straight tubular transparent container 8 made of quartz having a diameter of 1 cm is installed near the concentrating point of the concentrator 7 having a diameter of cm and 15 g of the catalyst 9
(Molybdenum disulfide supported on titanium dioxide with sodium carbonate added) is filled, and a 1: 1: 1 mixed gas of carbon dioxide, hydrogen and argon is passed at a flow rate of 6 ml / min to collect light. The reaction product obtained by irradiating the
Was analyzed using a gas chromatograph. As a result, about
12% of carbon dioxide was converted to carbon monoxide.
f.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、黒色で太陽光の吸収率がよく、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ー対策の面からも非常に有効であ
る。f. Effects of the Invention As described above, the present invention uses the sunlight collected by the solar concentrator to cause carbon dioxide to react with hydrogen on molybdenum sulfide filled in a transparent container to carry out monoxide oxidation. By using molybdenum sulfide catalyst, which converts to carbon, is black, has a good absorption rate of sunlight, can react at low temperature and atmospheric pressure, is inexpensive, has low toxicity, and is not poisoned by sulfur compounds. This enabled direct reduction of carbon dioxide by solar energy, which was difficult because the reaction temperature was high. Since this reaction is an absorption ergon reaction, the energy yield is good, and the product carbon monoxide can be used as it is as a fuel, or it can be converted to methanol or chemical raw materials that are in the spotlight as automobile fuels. Since it can be used, it is very effective from the aspect of global environment conservation and energy measures.
第1図第2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。FIG. 1 and FIG. 2 are schematic views showing an embodiment of the carbon dioxide gas reduction method of the present invention. In the figure, reference numeral 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 light collecting collector, 8 is a mixed gas of carbon dioxide, hydrogen and argon.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭55−51712(JP,A) 特開 昭63−80833(JP,A) ─────────────────────────────────────────────────── --Continued from the front page (56) References JP-A-55-51712 (JP, A) JP-A-63-80833 (JP, A)
Claims (4)
ン触媒を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 a molybdenum sulfide catalyst is installed near the focal point of a solar concentrator, and the condensed sunlight is transparent while a gas containing carbon dioxide and hydrogen is circulated in the transparent container. A method for reducing carbon dioxide, which comprises irradiating a catalyst in a container, reacting carbon dioxide with hydrogen on the catalyst, and converting the carbon dioxide into carbon monoxide.
熱器、樋形複合放物面鏡集光集熱器、樋形放物面鏡集光
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
載の炭酸ガスの還元方法。2. As a solar concentrator, a gutter-shaped flat mirror concentrator, a gutter-shaped compound parabolic concentrator, a gutter-shaped parabolic concentrator, and a gutter-shaped concentrator. A light collector that simulates an object mirror with a plane mirror.
A concentrating solar collector, such as a rotating parabolic mirror concentrator, a linear Fresnel lens concentrator, or a circular Fresnel lens concentrator, is used. The method for reducing carbon dioxide according to item 1.
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項記載の炭酸ガスの還元方法。3. A molybdenum sulfide catalyst as alumina, silica, activated carbon, zeolite, activated clay, bauxite,
The method for reducing carbon dioxide according to claim 1, wherein molybdenum disulfide supported on at least one carrier of silicon, silicon carbide, a metal oxide semiconductor, and a metal sulfide semiconductor is used.
塩を添加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 carbon dioxide gas reduction method according to claim 1, wherein supported molybdenum disulfide added with an alkali metal salt 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 JPH04198008A (en) | 1992-07-17 |
| JPH0723207B2 true 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) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116239435B (en) * | 2023-03-17 | 2024-07-30 | 华东师范大学 | A method for constructing a catalyst-free 185nm photochemical reaction system and its 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 |
Family Cites Families (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
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04198008A (en) | 1992-07-17 |
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