JPH04235738A - Catalyst for reducing carbon dioxide - Google Patents
Catalyst for reducing carbon dioxideInfo
- Publication number
- JPH04235738A JPH04235738A JP3103218A JP10321891A JPH04235738A JP H04235738 A JPH04235738 A JP H04235738A JP 3103218 A JP3103218 A JP 3103218A JP 10321891 A JP10321891 A JP 10321891A JP H04235738 A JPH04235738 A JP H04235738A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- carbon dioxide
- ruthenium
- fiber
- reactor
- 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.)
- Withdrawn
Links
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 239000003054 catalyst Substances 0.000 title claims abstract description 46
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims abstract description 28
- 239000001569 carbon dioxide Substances 0.000 title claims abstract description 27
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 claims abstract description 19
- 229910052707 ruthenium Inorganic materials 0.000 claims abstract description 18
- 239000012210 heat-resistant fiber Substances 0.000 claims abstract description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000835 fiber Substances 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 238000011084 recovery Methods 0.000 abstract description 3
- 230000003197 catalytic effect Effects 0.000 abstract description 2
- 239000000377 silicon dioxide Substances 0.000 abstract description 2
- 239000008246 gaseous mixture Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 13
- 238000006722 reduction reaction Methods 0.000 description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 8
- 229920000049 Carbon (fiber) Polymers 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- QZPSXPBJTPJTSZ-UHFFFAOYSA-N aqua regia Chemical compound Cl.O[N+]([O-])=O QZPSXPBJTPJTSZ-UHFFFAOYSA-N 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Carbon And Carbon Compounds (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は炭酸ガス還元用触媒に関
し、特に炭酸ガス還元酸素回収システムの炭酸ガス還元
反応に用いられ触媒に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a catalyst for reducing carbon dioxide gas, and more particularly to a catalyst used in a carbon dioxide reduction reaction in a carbon dioxide reduction oxygen recovery system.
【0002】0002
【従来の技術】従来の炭酸ガス還元法の一態様を図1に
よって説明する。図1において、反応器1に直径3mm
、長さ3mmのペレット状ルテニウム触媒2(担持体:
アルミナ)が一定量充填されている。温度調整器3によ
りルテニウム触媒2層を約400℃に加温する。ルテニ
ウム触媒2層が約400℃に達した後、炭酸ガス4及び
水素ガス5をガス混合器6へ流入させ、その混合ガスを
反応器1へ送ることにより炭酸ガスが水素ガスにより還
元され、メタンガス7と水8が生成する。なお、反応器
1へのルテニウム触媒2充填量及び充填体積はそれぞれ
340g、340cm3 である。2. Description of the Related Art One aspect of a conventional carbon dioxide reduction method will be explained with reference to FIG. In Figure 1, reactor 1 has a diameter of 3 mm.
, 3 mm long pelleted ruthenium catalyst 2 (support:
Alumina) is filled with a certain amount. The two layers of ruthenium catalyst are heated to about 400° C. by the temperature regulator 3. After the two layers of ruthenium catalyst reach approximately 400°C, carbon dioxide gas 4 and hydrogen gas 5 are flowed into gas mixer 6, and the mixed gas is sent to reactor 1, whereby carbon dioxide gas is reduced by hydrogen gas, and methane gas 7 and water 8 are produced. The amount and volume of the ruthenium catalyst 2 packed into the reactor 1 were 340 g and 340 cm3, respectively.
【0003】0003
【発明が解決しようとする課題】従来の炭酸ガス還元法
には下記のような欠点がある。
(1)炭酸ガス還元用触媒として使用しているルテニウ
ムは担持体としてアルミナペレットが用いられているた
め重量が大きい。
(2)従って宇宙船用として炭酸ガス還元酸素回収シス
テムを宇宙往還機で打ち上げる場合不利である。
(3)ペレット状触媒は比表面積が小さいため、その一
部が被毒された場合反応率が低下する。[Problems to be Solved by the Invention] Conventional carbon dioxide reduction methods have the following drawbacks. (1) Ruthenium used as a carbon dioxide reduction catalyst is heavy because alumina pellets are used as a support. (2) Therefore, it is disadvantageous when launching a carbon dioxide reduction oxygen recovery system for spacecraft using a spacecraft. (3) Since the pellet-shaped catalyst has a small specific surface area, the reaction rate will decrease if a part of it is poisoned.
【0004】本発明は以上の問題点を解決するため、ル
テニウム触媒の軽量化及び比表面積を大きくして長寿命
化を図ることのできる炭酸ガス還元用触媒を提供しよう
とするものである。[0004] In order to solve the above-mentioned problems, the present invention aims to provide a catalyst for reducing carbon dioxide gas, which can be made lighter and have a larger specific surface area, thereby extending its life.
【0005】[0005]
【課題を解決するための手段】本発明は耐熱性繊維にル
テニウムを担持してなることを特徴とする炭酸ガス還元
用触媒である。[Means for Solving the Problems] The present invention is a catalyst for reducing carbon dioxide gas, which is characterized by having ruthenium supported on heat-resistant fibers.
【0006】本発明において使用される耐熱性繊維とし
てはアルミナ繊維、シリカ繊維、活性炭繊維などがあげ
られる。[0006] Examples of the heat-resistant fibers used in the present invention include alumina fibers, silica fibers, and activated carbon fibers.
【0007】[0007]
【作用】本発明の炭酸ガス還元用触媒は従来のルテニウ
ム金属をナルミナペレットに添着させたルテニウム触媒
と比較すると、
(1)触媒として同程度の性能をもたせるためには、本
発明触媒は従来触媒の約1/7の重量でよく、大幅な重
量軽減が可能となる。
(2)本発明は触媒の比表面積ははるかに大きくなり、
触媒の長寿命化が可能となる。
(3)宇宙船用触媒として、本発明触媒は上記(1)及
び(2)項に示す理由から極めて有利となる。[Function] When compared with the conventional ruthenium catalyst in which ruthenium metal is impregnated with alumina pellets, the catalyst for carbon dioxide reduction of the present invention has the following characteristics: (1) In order to have the same performance as a catalyst, the catalyst of the present invention has to It only requires about 1/7 of the weight of the catalyst, making it possible to significantly reduce the weight. (2) In the present invention, the specific surface area of the catalyst is much larger,
It is possible to extend the life of the catalyst. (3) As a catalyst for spacecraft, the catalyst of the present invention is extremely advantageous for the reasons shown in items (1) and (2) above.
【0008】[0008]
【実施例】以下、前記図1のフローに従って本発明触媒
の一実施例の効果を立証する。図1において、反応器1
に活性炭素繊維を担持体とするルテニウム触媒2を充填
する以外は、前記した従来技術と同様に操作した。EXAMPLE Hereinafter, the effect of an example of the catalyst of the present invention will be demonstrated according to the flow shown in FIG. 1. In FIG. 1, reactor 1
The operation was carried out in the same manner as in the prior art described above, except that the ruthenium catalyst 2 having activated carbon fiber as a carrier was filled in the ruthenium catalyst.
【0009】炭酸ガス還元反応はガスモル比(H2 /
CO2 )を4.1以上にすることにより反応率約10
0%であった。なお本試験で反応器1に充填したルテニ
ウム触媒2の重量は50gであり、従来触媒(担体:ア
ルミナペレット、触媒成分:ルテニウム)は反応率約1
00%にするためには約350g必要であた。[0009] The carbon dioxide reduction reaction depends on the gas molar ratio (H2/
By increasing the CO2) to 4.1 or higher, the reaction rate is approximately 10
It was 0%. In this test, the weight of the ruthenium catalyst 2 packed into the reactor 1 was 50 g, and the conventional catalyst (carrier: alumina pellets, catalyst component: ruthenium) had a reaction rate of about 1.
Approximately 350g was required to achieve 00%.
【0010】この試験での試験条件は次の通りである。
・炭酸ガス流入量・・・・0.35l/min ・水素
ガス流入量・・・・1.44l/min ・触媒充填体
積 ・・・・340cm3 (40φ×270mm)
・反応器内圧力 ・・・・1kg/cm2 G ・炭
酸ガス還元率・・・・反応器出口ガスをガスクロマトグ
ラフで分析The test conditions for this test are as follows. - Carbon dioxide gas inflow rate...0.35 l/min - Hydrogen gas inflow rate...1.44 l/min - Catalyst packing volume...340cm3 (40φ x 270mm) - Reactor internal pressure...・1kg/cm2 G ・Carbon dioxide reduction rate... Analyze the reactor outlet gas with a gas chromatograph
【0011】なお、上記試験で使用した本発明実施例触
媒は下記のようにして製造されたものである。活性炭素
繊維(線径1〜10μm :市販品)を硝酸10%溶液
中で2〜3時間加熱処理後濾過水洗し乾燥する。ルテニ
ウムを王水で溶解後、加熱濃縮して塩酸々性とし、温水
を加えて約80mlとする。この溶液に前記の乾燥した
活性炭繊維を加える。次いでこの溶液にホルマリン(3
7wt%)を約8ml加えた後、NaOH溶液(30w
t%)を溶液が弱アルカリ性を示すまで加える。その後
、活性炭繊維を溶液から取出し、水洗した後120〜1
50℃で乾燥する。以上の工程によって製造したものを
実施例触媒として用いた。The catalyst of the present invention used in the above test was produced in the following manner. Activated carbon fibers (wire diameter 1 to 10 μm: commercially available) are heated in a 10% nitric acid solution for 2 to 3 hours, filtered, washed with water, and dried. After dissolving ruthenium in aqua regia, heat and concentrate to make it hydrochloric-acidic, and add warm water to make about 80 ml. Add the dried activated carbon fibers to this solution. Next, formalin (3
After adding about 8 ml of NaOH solution (30w
t%) until the solution becomes slightly alkaline. After that, the activated carbon fibers were taken out from the solution, washed with water, and then
Dry at 50°C. The catalyst produced by the above steps was used as an example catalyst.
【0012】0012
【発明の効果】宇宙船内で人の呼吸により発生した炭酸
ガスを還元して、酸素を回収するシステムを、宇宙往還
機で打上げる場合、炭酸ガス還元用触媒の重量軽減及び
触媒を交換する頻度を少なくするために触媒の長寿命化
が不可欠であり、本発明の触媒は、次の効果を有する。
(1)本発明触媒は、従来品の1/7重量で、従来品と
同程度の触媒性能を有する。
(2)本発明品は触媒の比表面が従来品より大となり、
触媒の長寿命化が可能となって、触媒交換頻度が少なく
なり、乗員の作業軽減が可能となる。[Effect of the invention] When a spacecraft launches a system that recovers oxygen by reducing carbon dioxide generated by human breathing inside a spacecraft, the weight of the carbon dioxide reduction catalyst is reduced and the frequency of catalyst replacement is required. It is essential to extend the life of the catalyst in order to reduce the amount of carbon dioxide, and the catalyst of the present invention has the following effects. (1) The catalyst of the present invention is 1/7 the weight of a conventional product and has catalytic performance comparable to that of a conventional product. (2) The product of the present invention has a larger specific surface of the catalyst than the conventional product,
This makes it possible to extend the life of the catalyst, reducing the frequency of catalyst replacement and reducing the workload of the crew.
【図1】炭酸ガス還元反応工程の説明図。FIG. 1 is an explanatory diagram of a carbon dioxide gas reduction reaction step.
Claims (1)
ることを特徴とする炭酸ガス還元用触媒。1. A catalyst for reducing carbon dioxide gas, characterized by comprising ruthenium supported on heat-resistant fibers.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3103218A JPH04235738A (en) | 1991-01-18 | 1991-01-18 | Catalyst for reducing carbon dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3103218A JPH04235738A (en) | 1991-01-18 | 1991-01-18 | Catalyst for reducing carbon dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04235738A true JPH04235738A (en) | 1992-08-24 |
Family
ID=14348364
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3103218A Withdrawn JPH04235738A (en) | 1991-01-18 | 1991-01-18 | Catalyst for reducing carbon dioxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04235738A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6180396B1 (en) * | 1998-03-13 | 2001-01-30 | Research Institute Of Innovative Technology For The Earth | Carbon producing apparatus utilizing biomass |
JP4598994B2 (en) * | 2000-06-30 | 2010-12-15 | 三菱重工業株式会社 | Carbon dioxide reduction equipment |
JP2011241182A (en) * | 2010-05-19 | 2011-12-01 | Tokyo Gas Co Ltd | Method for synthesizing methane from carbon dioxide and hydrogen |
-
1991
- 1991-01-18 JP JP3103218A patent/JPH04235738A/en not_active Withdrawn
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6180396B1 (en) * | 1998-03-13 | 2001-01-30 | Research Institute Of Innovative Technology For The Earth | Carbon producing apparatus utilizing biomass |
JP4598994B2 (en) * | 2000-06-30 | 2010-12-15 | 三菱重工業株式会社 | Carbon dioxide reduction equipment |
JP2011241182A (en) * | 2010-05-19 | 2011-12-01 | Tokyo Gas Co Ltd | Method for synthesizing methane from carbon dioxide and hydrogen |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 19980514 |