JPS6044044A - Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound - Google Patents
Internal shortcircuit battery type catalyst for oxidizing or reducing organic compoundInfo
- Publication number
- JPS6044044A JPS6044044A JP58151132A JP15113283A JPS6044044A JP S6044044 A JPS6044044 A JP S6044044A JP 58151132 A JP58151132 A JP 58151132A JP 15113283 A JP15113283 A JP 15113283A JP S6044044 A JPS6044044 A JP S6044044A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- reaction
- exchange resin
- ion exchange
- conductive powder
- 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
- 239000003054 catalyst Substances 0.000 title claims abstract description 42
- 230000001590 oxidative effect Effects 0.000 title claims abstract description 11
- 150000002894 organic compounds Chemical class 0.000 title description 3
- 239000000843 powder Substances 0.000 claims abstract description 24
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000003456 ion exchange resin Substances 0.000 claims abstract description 17
- 229920003303 ion-exchange polymer Polymers 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 10
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 5
- 150000001875 compounds Chemical class 0.000 claims abstract description 4
- 239000007800 oxidant agent Substances 0.000 claims abstract description 3
- 239000004020 conductor Substances 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 abstract description 35
- 238000007254 oxidation reaction Methods 0.000 abstract description 21
- 230000003647 oxidation Effects 0.000 abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 9
- 239000003792 electrolyte Substances 0.000 abstract description 8
- 230000009467 reduction Effects 0.000 abstract description 8
- 239000011347 resin Substances 0.000 abstract description 7
- 229920005989 resin Polymers 0.000 abstract description 7
- 239000011230 binding agent Substances 0.000 abstract description 5
- 239000007795 chemical reaction product Substances 0.000 abstract description 5
- -1 polytetrafluoroethylene Polymers 0.000 abstract description 4
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 abstract description 3
- 239000007864 aqueous solution Substances 0.000 abstract description 3
- 229910052731 fluorine Inorganic materials 0.000 abstract description 3
- 239000011737 fluorine Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 239000012153 distilled water Substances 0.000 abstract description 2
- 239000010416 ion conductor Substances 0.000 abstract description 2
- 230000002829 reductive effect Effects 0.000 abstract description 2
- 239000007784 solid electrolyte Substances 0.000 abstract description 2
- 238000001035 drying Methods 0.000 abstract 1
- 238000004898 kneading Methods 0.000 abstract 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 abstract 1
- 239000004810 polytetrafluoroethylene Substances 0.000 abstract 1
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 12
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 238000006722 reduction reaction Methods 0.000 description 8
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 6
- 239000000376 reactant Substances 0.000 description 6
- 239000003115 supporting electrolyte Substances 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 5
- 238000003487 electrochemical reaction Methods 0.000 description 5
- 150000002500 ions Chemical class 0.000 description 5
- 238000001179 sorption measurement Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 239000007858 starting material Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- AZQWKYJCGOJGHM-UHFFFAOYSA-N 1,4-benzoquinone Chemical compound O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- ISAOCJYIOMOJEB-UHFFFAOYSA-N benzoin Chemical compound C=1C=CC=CC=1C(O)C(=O)C1=CC=CC=C1 ISAOCJYIOMOJEB-UHFFFAOYSA-N 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 238000005341 cation exchange Methods 0.000 description 2
- 239000011790 ferrous sulphate Substances 0.000 description 2
- 235000003891 ferrous sulphate Nutrition 0.000 description 2
- 239000002638 heterogeneous catalyst Substances 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 2
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 235000017166 Bambusa arundinacea Nutrition 0.000 description 1
- 235000017491 Bambusa tulda Nutrition 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 244000082204 Phyllostachys viridis Species 0.000 description 1
- 235000015334 Phyllostachys viridis Nutrition 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 244000028419 Styrax benzoin Species 0.000 description 1
- 235000000126 Styrax benzoin Nutrition 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 235000008411 Sumatra benzointree Nutrition 0.000 description 1
- 102220585033 Transcription factor Sp6_N12S_mutation Human genes 0.000 description 1
- 125000002777 acetyl group Chemical class [H]C([H])([H])C(*)=O 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 238000005882 aldol condensation reaction Methods 0.000 description 1
- 229910001854 alkali hydroxide Inorganic materials 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- RAWGYCTZEBNSTP-UHFFFAOYSA-N aluminum potassium Chemical compound [Al].[K] RAWGYCTZEBNSTP-UHFFFAOYSA-N 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 238000005349 anion exchange Methods 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 239000011425 bamboo Substances 0.000 description 1
- 229960002130 benzoin Drugs 0.000 description 1
- 125000001797 benzyl group Chemical group [H]C1=C([H])C([H])=C(C([H])=C1[H])C([H])([H])* 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 125000002843 carboxylic acid group Chemical group 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 150000001860 citric acid derivatives Chemical class 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- IMBKASBLAKCLEM-UHFFFAOYSA-L ferrous ammonium sulfate (anhydrous) Chemical compound [NH4+].[NH4+].[Fe+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O IMBKASBLAKCLEM-UHFFFAOYSA-L 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 235000019382 gum benzoic Nutrition 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 229910001410 inorganic ion Inorganic materials 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 150000007522 mineralic acids Chemical group 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000002825 nitriles Chemical class 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 230000002940 repellent Effects 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 1
- 229910001948 sodium oxide Inorganic materials 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 125000000626 sulfinic acid group Chemical group 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- TXEYQDLBPFQVAA-UHFFFAOYSA-N tetrafluoromethane Chemical compound FC(F)(F)F TXEYQDLBPFQVAA-UHFFFAOYSA-N 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
Landscapes
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は内部短絡電池式触媒に開力るものである。ざら
に詳しくは、酸化体を電解還元すのに有効な電子伝導体
粉末と還元体を電解酸化するのに有効/i−電了電導伝
導体粉イオン伝導体どしてのイオン交換樹脂の粉末bt
、<は短iMIflとの混合物をフッ素樹脂からなる結
着剤で粘着してなることを特徴どりるイj Il化合物
を酸化もしくは還元するための内部う、0絡電池式触媒
に関するしのでdする。DETAILED DESCRIPTION OF THE INVENTION The present invention is directed to internally shorted cell catalysts. For more details, see Electron conductor powder effective for electrolytically reducing oxidizers and Electron conductor powder effective for electrolytically oxidizing reductants/i- Electron conductor powder Ion exchange resin powder as an ion conductor bt
, < is characterized by being made by adhering a mixture of Il and MIfl with a binder made of fluororesin. .
化学反応の多くは、酸化還元反応である。1′なりら、
)W元体が酸化される反応が酸化反応rあり、酸化体が
還元される反応が)!元反応である。Many chemical reactions are redox reactions. 1',
) There is an oxidation reaction r in which the W element is oxidized, and there is a reaction in which the oxidized form is reduced)! This is the original reaction.
ノj、電池イ1−どの電気化学装置にお()る電気化学
反応し酸化jW元反応である。すなわち、電気化学駅1
4には必ずカソードとアノードど電解質とが存在覆るが
、ツノソード反応はすべて)!元反応であり、アノード
反応はJ−べて酸化反応である。The electrochemical reaction in any electrochemical device is an oxidation reaction. That is, electrochemical station 1
4, there is always an electrolyte at the cathode and anode, but all hornsode reactions)! The anode reaction is a J-beta oxidation reaction.
通常の化学反応と電気化学反応との差は、前者で・は、
少くとも児用・1ノの1−では電子の授受が起らないの
に対し、後右では電子の授受が起り、電流が外部回路を
流れるという点にある。ところが、通常の化学反応であ
ってb、微視的にみると、実1.1電気化学反応である
か、電気化学反応どして説明り−るど反応メカニズムが
よく理解できる場合も多々ある。例えば活性炭を触媒ど
しで、水の存右下で二酸化イAつど酸素とを反応させる
と、硫酸が生成するが、この反応は見掛けの上では通常
の接触IL学反応であるが、微視的にみると、活性炭の
酸素の吸着リイトでは、次のような酸素の電解還元反応
が起り、
1・’2Q、・ 1211’ ト2(+−1120(1
)活性炭の丁^η化イΔ「″ノの吸着1」イ1〜ではS
O;、1211;40
+SO,,2−+41−(” +2e−(2)イする電
解酸化反応が起り、全体どしては1、’ 202 +
802 +1」20→11.: 804 (3>なる反
応が起るど32明されている。JIA言Jると、活tI
l l火十で、酸素−二酸化イAつ電池が形成され、こ
れが電子伝導1)1の活性炭で内部短絡されているどど
らえることができる。この場合には、反応初期には、二
:酸化イAつが水に溶けて生成する亜硫酸が支持電解質
としてff!llき、(2)式の反応がある稈痘進んだ
のちは、硫酸が支1!r電解質どして働いていると考え
ることができる。The difference between a normal chemical reaction and an electrochemical reaction is that in the former case,
At least in the child's 1-1-, no exchange of electrons occurs, whereas in the rear right, exchange of electrons occurs and current flows through the external circuit. However, even though it is a normal chemical reaction, when viewed microscopically, there are many cases where the reaction mechanism can be better understood by explaining it as an electrochemical reaction or an electrochemical reaction. . For example, when activated carbon is reacted with oxygen and carbon dioxide in the lower right of the presence of water using a catalyst, sulfuric acid is produced.This reaction is apparently a normal contact IL reaction, but it is microscopic. Generally speaking, in the oxygen adsorption litite of activated carbon, the following electrolytic reduction reaction of oxygen occurs: 1・'2Q,・1211′
) Activated carbon's adsorption 1 is S.
O;,1211;40 +SO,,2-+41-(" +2e-(2)) An electrolytic oxidation reaction occurs, and the total is 1,' 202 +
802 +1” 20→11. : 804 (3) It is clear that the following reaction occurs.
In the heat, an oxygen-dioxide cell is formed, which can be internally shorted with activated carbon that conducts electrons. In this case, in the early stage of the reaction, sulfurous acid produced by dissolving dioxide in water acts as a supporting electrolyteff! After the reaction of formula (2) has progressed, sulfuric acid is the main ingredient! You can think of it as working as an r-electrolyte.
その他、例えば特公昭5(1−40305@には、撥水
処1りIを施した活性炭を触媒にして、硫化す1−リウ
ムの水溶液と空気とを作用させると、単体イオウと水酸
化ナトリウムが生成するとし、この反応(6式)は次の
(4)式の電解酸化酸1.ト8、どく!))式の電解還
元反応の絹合せであるど説明さ4LCいる。In addition, for example, in the Japanese Patent Publication No. 5 (1-40305@), when an aqueous solution of 1-lium sulfide is reacted with air using activated carbon treated with water repellent treatment as a catalyst, elemental sulfur and sodium hydroxide are produced. This reaction (equation 6) can be explained as a combination of the electrolytic oxidizing acid 1.8, doku!)) electrolytic reduction reaction of the following equation (4).
52−−−)SO+2e−C4)
21120+02 +4e−−+ 4011 (5)2
Nil、: S + 2112 0 102−+ 28
n+ 4N、1Oll (6)なお、L記引例(、二(
I、liiし)説明されてい/I−い(jれども、この
反応し1.反応V月す1には、N12 Sを、(5)式
の反応がある程度進んだのちに(L、水酸化ナトリウム
を支持電解質とした酸m j、I!1化(Aつ電池を活
性炭で内部短絡ざ11て起っに反応と説明することが可
能である。52---) SO+2e-C4) 21120+02 +4e--+ 4011 (5)2
Nil,: S + 2112 0 102-+ 28
n+ 4N, 1Oll (6) In addition, L citation example (, 2 (
I,lii) has not been explained/I-(jHowever, in this reaction, N12S is added to the reaction V, and after the reaction of equation (5) has proceeded to a certain extent, (L, water) It is possible to explain the reaction as occurring when an internal short-circuit occurs in an activated carbon battery using sodium oxide as a supporting electrolyte.
このように、電子伝導t9をltりる話す1炭を不均一
系触媒として、見用1〕+1.1.11 イ、−イ、化
学反応【゛あるが、微視的にみると、実は電気化学反応
で・ある反応例として、例えば、持久nn 52−31
H1823’3 L: kl、次のようなものが掲げら
れている。In this way, if we talk about electron conduction t9 using 1 carbon as a heterogeneous catalyst, we can see that there is a chemical reaction [゛, but microscopically, As an example of an electrochemical reaction, for example, endurance nn 52-31
H1823'3 L: kl, the following are listed.
(イ)空気によるチA硫酸J1〜す・”ノlzの硫酸−
11−リウムへの酸化、([1)空気にJ、る硫酸第一
鉄:または硫酸第一鉄アンモニウムの硫酸第二!i′J
11\の酸化、(ハ)空気によるハイド[1キノンのキ
ンじドロンへの酸化、(ニ)空気によるフェノールの酸
化、(ホ)空気によるベンズアルYじドの安つj′rl
酸への酸化、(へ)水素ガスにJ=る硝酸1Rの銀への
還元。(a) Sulfuric acid of sulfuric acid J1-S.
Oxidation to 11-lium, ([1) J in air, ferrous sulfate: or ferrous ammonium sulfate to ferrous sulfate! i′J
11\ oxidation, (c) oxidation of hyde [1 quinone to quinedrone with air, (d) oxidation of phenol with air, (e) oxidation of benzal Yd with air
Oxidation to acid, (to) reduction of nitric acid 1R to hydrogen gas to silver.
いずれにしても、微視的にz777こ電池の内部フ、0
絡現客によって化学反応を進行さ1!−J−うとするた
めには、触媒が電子伝導性をイアする固体であh、しか
も支持電解質が共存していることが不可欠で(偽る。In any case, microscopically, the internal battery of the z777 battery, 0
A chemical reaction is progressed by the interaction customer 1! -J- In order to achieve this, it is essential that the catalyst be a solid that exhibits electronic conductivity, and that a supporting electrolyte coexist (false).
従来、支持電解質どしては、各個別反応に応じて、各々
個別に反応以前の出発物質である無機の1為、酸もしく
は水酸化アルカリか、反応の)V行とともに生成する反
応生成物が流用されていたということができる。これに
対lノーで、殊にイrlj3を化学反応においては、一
般に反応の出発物質も反応生成物もイオン伝導性を示さ
ず、電解質としての機能を果さないので、別途に無機の
支持電解質を混入させる必要が出てくる。Conventionally, the supporting electrolyte has been used for each individual reaction, depending on whether it is an inorganic acid or alkali hydroxide that is the starting material before the reaction, or a reaction product that is formed together with the V line (of the reaction). It can be said that it was appropriated. On the other hand, in the chemical reaction of Irlj3, in general, neither the starting material nor the reaction product exhibits ionic conductivity and does not function as an electrolyte, so a separate inorganic supporting electrolyte is used. It becomes necessary to mix in.
5−
ところが、無機の支持電解質を添加した場合には1反応
終了後に目的反応生成物と無機の支持電解質どを分ビレ
lることが入さ/fガ題となる。5- However, when an inorganic supporting electrolyte is added, it becomes a problem that the desired reaction product and the inorganic supporting electrolyte must be separated after one reaction is completed.
本発明はかかる問題を解決せんとするものであり、酸化
杯を電解遅元づるのに有ダ)な電子伝導体粉末と還元体
を電解酸化するのにイj効な電子伝導体粉末とイオン伝
導体としてのイオン交換樹脂の粉末らしくは知繊紺との
混合物をフッ素樹脂からなる結着剤で結盾してなること
を特徴とJ−る有機化合物を醸化Jるかもしくは還元す
るための触媒を提供りるらのである。The present invention aims to solve such problems, and provides an electron conductor powder that is effective in electrolytically oxidizing an oxidized cup, and an electron conductor powder and ions that are effective in electrolytically oxidizing a reductant. The ion-exchange resin powder used as a conductor is characterized by being made by binding a mixture with Chisen-Kon blue with a binder made of fluororesin.It is used for fermentation or reduction of organic compounds. It provides a catalyst for this.
すなわち、かかる触媒では、イオン交換樹脂に含水させ
さえすればイオン交換樹脂が固体電解質ど()て■能1
−るので、この触媒を使用して化学反応を起させて19
られる反応生成物と電解質との分離1は全く容易となる
。Jなわちこの触媒は電解質を含めた不均一系触媒であ
る。In other words, with such a catalyst, as long as the ion exchange resin is hydrated, the ion exchange resin can be used as a solid electrolyte.
- Therefore, using this catalyst to cause a chemical reaction, 19
The separation 1 between the reaction product and the electrolyte becomes quite easy. J This catalyst is a heterogeneous catalyst including an electrolyte.
一方、本発明にかかる触媒は、それ自体電解質を保持j
ノでいるというM味から、内部短絡された完6′、シた
電池としてとらえることができるので、6−
[内部短絡電池式触媒1ど定義・Jく)ことにする。On the other hand, the catalyst according to the present invention itself retains the electrolyte.
Since it can be regarded as an internally short-circuited complete battery, it will be defined as 6-[Definition of internally short-circuited battery type catalyst 1 etc.].
このような明確/j触媒段訂思想(,1、従来なか−)
I、:3゜この内部短絡電池式触A;に用いらねる電子
11、力性を有しかつ触媒活性を示す粉末月利とし−U
fil、当然使用目的によって異4(〕−Cりる/l
<、通例(J金属、カーボンあるいはカーボン)こ↑)
ハスをIQ 1.’l l、たものが適しているが、一
部のスピンルp1す酸化物あるいはペロジスカイ1〜型
酎化物の如さ金属酸11c物やホウ化金属のよう<iか
<’Lりの電子伝導性を示c1化合物を使用できること
もある。Such a clear/j catalyst stage revision thought (, 1, conventionally -)
I: 3゜Electron 11 used in this internal short-circuit battery type catalyst A; Powder monthly rate which has power and shows catalytic activity -U
fil, of course it varies depending on the purpose of use4(]-Criru/l
<, usually (J metal, carbon or carbon) ↑)
Lotus IQ 1. 'l l, etc. are suitable, but some spindle p1 oxides or perodiskii type 1~ type citrates, metal acids 11c, metal borides, etc. with <i or <'L electron conductivity are suitable. In some cases, c1 compounds can be used.
あるいill J、た、アルミ−ノ1ゝ)シリカの如き
、でれ自体電子伝導i生をもたイτい10体に、金属を
IIl持さけたものを用いること−bできる。その他、
これらの触媒活性を示す粉末と触媒活性を示さないが、
゛電子伝導性の向りに寄りJる」、うな44 ′J’l
を混合することも有効な揚台がある。Alternatively, it is possible to use a material such as silica, which itself has electron conductivity, with a metal added to it. others,
These powders exhibit catalytic activity and powders that do not exhibit catalytic activity.
``Move toward electron conductivity'', Una44 'J'l
There is also an effective frying platform for mixing.
さらには、この電子伝IJt’4をイjし、触媒病t’
lを示す粉末は、酸化体の)ψ元反応−13J、び還元
体の酸化反応にそれぞれ選択性を有Jる異種材料の混合
物にすることが非常に有効であるが、場合によっては同
一の粉末にしてもかまわない。Furthermore, I jj this electronic transmission IJt'4, catalytic disease t'
It is very effective to make the powder showing l by using a mixture of different materials that have selectivity for the ψ elementary reaction of the oxidant and the oxidation reaction of the reductant. You can also make it into powder.
内部う、0組電池式触媒の他の構成(イ利で・あるイオ
ン交換樹n[7どしCは、カチAン交換型のものとアニ
オン交換メ(1!のものがある。カチオン交換樹脂とし
U k:1、スブレンージビニルベンロン共重合捧ある
い1.1パーフロ[iカーボンの如き含フツ素高分子を
ベースにし、これにスルフ4ン酎阜、カルボン酸基ある
いは両省を導入したものが適しているが、本発明(31
これらに限定ηるものではない。この力チΔン交1条樹
脂の移動づるイオン(ま水素イオンであろ1゜
アーΔン交換樹11ftどして11、ポリスヂレン系母
核(5:、アントニウム塩をアミン0シ<はジエチレン
トすj7ミンのJ:うなアミンを交%I! 1;!どし
て導入しIこ6のをアルミカリ(−QJI I甲して、
水酸イオン移動型どじノご1−)のを−用い1′1ぼJ
−い1゜これらの(Aン交換樹脂(J5、粉末状の6の
か知識1t(l状のものが適しCいる。粉末状の間合に
は、数十ミラ1]ン以下の粒径のものがJ、い。短繊維
状のものは、直径が故ミクf]ン、長さが数ll1m以
下のものがにい。Internal cavity, 0 set Other configurations of battery-type catalysts (I) Some ion exchange trees N[7 and C are available in cation exchange type and anion exchange type (1!).Cation exchange type The resin is based on a fluorine-containing polymer such as U k: 1, sulfuric acid, divinylbenron copolymer, or 1.1 perfluorocarbon, and is added with sulfuric acid, carboxylic acid groups, or both. Although the introduced one is suitable, the present invention (31
It is not limited to these. Ions (or hydrogen ions) that move through the resin through the 1° arc Δn exchange tree 11, polystyrene mother core (5:, anthonium salt, amine 0, diethylene j7 min J: Exchange amine with % I! 1;! and introduce I this 6 with aluminum potassium (-QJI I
Hydroxyl ion transfer type dojinogo 1-) using 1'1 BoJ
-1゜These (A exchange resins (J5, 6 in powder form) are suitable (L-shaped ones are suitable). The short fibrous ones are those with a diameter of 1.5 mm and a length of several 1 m or less.
カチオン交換樹脂を用いるか)′二Aン交操樹脂を用い
るかは、対象どイする反応系によって適官選4R−dる
必要がある。Whether to use a cation exchange resin or a 2-A crosslinked resin must be selected depending on the reaction system to be treated.
内部短絡電池式触媒のbうひどつの構成+A PI 7
’あるフッ素樹脂結着剤は、電子伝導111を有し、か
つ触媒活性を承り粉末および−(Aン交換樹flliを
結着するという機O1iの曲に、内部短絡′rIi池式
触媒に撥水性を付与するという機能を5 ’4’Hl、
”Cいる。Fjなわち内部短絡電池式触媒1.;1 、
液体の反応物質と気体の反応物質どを出発原料にすろ反
応に冶しCいるが、内部短絡電池式触媒/I<全く親水
11の場合には、液体の反応物質に被覆さ1′1尽さ4
′;て、気体の反応物質の吸着サイトがなくなってしま
うのに対し、部分的に撥水性を有していると、気1本反
応物質の吸着サイ1−および液体反応物質の吸着サイ1
−の双方が確保されるの−C1反応がよりスムースに進
みやすい。Internal short-circuit battery type catalyst b excellent configuration + A PI 7
A certain fluororesin binder has electron conductivity 111 and has catalytic activity to bind the powder and -(A exchange tree flli), while internal short circuits 'rIi repel the pond-type catalyst. 5'4'Hl has the function of imparting aqueous properties.
"C.Fj, i.e. internal short circuit battery type catalyst 1.;1,
A liquid reactant and a gaseous reactant are used as starting materials to carry out a reaction, but if the internal short-circuited cell catalyst/I<11 is completely hydrophilic, the liquid reactant is coated with 1'1'. Sa4
′;, whereas adsorption sites for gaseous reactants are lost, if there is partial water repellency, adsorption sites for gas 1 reactant and adsorption sites 1 for liquid reactants are eliminated.
- If both of these conditions are ensured, the -C1 reaction tends to proceed more smoothly.
フッ素樹脂結着剤とし−Cは、出発)(応物質【こ侵さ
れにくいという性質と耐熱性がよ(戸ということ9−
と電池触媒の他の椙成月料を被覆1〕尽さ2=(いとい
う意味から、殊にポリ 4フツ化1’i =1−1ノン
が7iu 38であるが、この相場11に限定1Jるt
〕のではイ1い。As a fluororesin binder, -C is the starting material. = (From the meaning of "I", especially polytetrafluoride 1'i = 1-1 non is 7iu 38, but this price is limited to 11J
].
内部短絡電池式触媒の形状として(1、粒状、シート状
、筒状あるいはハニカl\状等いか(47る形状にする
ことも可能である。あるい(L土に内部9.’O8B電
池1(触媒のδ(b成4A l’ilの混合物を金属の
絹ル)るいはエキスパンデツ1:メタルと一体に成形す
ることにJ: −> T G讃械的強度の増大を図るこ
ともtI効4f揚合がある。The shape of the internal short-circuit battery type catalyst (1, granular, sheet-like, cylindrical, honeycomb, etc.) is also possible. (It is also effective to increase the mechanical strength by molding the catalyst δ (b-formation 4A l'il mixture into metal silk) or by expanding it into one piece with the metal.) There is a 4f lift.
本発明にかかる内部短絡電池式触kl+は、水が必須で
あるところから、水溶液中の(11幾化合物を酸素によ
って酸化さけたり、水素にJ、って還元さIJたりする
反応に特に適しているが、イの用途は、むしろ今後拡大
されていくものと考えられる。Since water is essential, the internal short-circuit battery-type catalyst kl+ according to the present invention is particularly suitable for reactions such as avoiding oxidation of compound (11) in aqueous solution with oxygen, or reducing IJ to hydrogen. However, it is thought that its uses will expand in the future.
水は水蒸気という形で供給〕−る方が適していることも
ある。ただ内部短絡電池式触媒は、イオン交換樹脂を内
包している関係−1、無機−イオンが共存していると、
イオン置換が起り、イオン交換樹脂の中での移動イオン
が水素イオンムしくは水酸10−
ィA−ン以外のものになるので不都合であり、無量イオ
ンを含まない反応系に適用するのが望ましい。In some cases, it is more suitable to supply water in the form of steam. However, internally shorted battery-type catalysts contain ion-exchange resin, so if inorganic ions coexist,
This is inconvenient because ion substitution occurs and the ions transferred in the ion exchange resin become hydrogen ions or other than 10-A-1 hydroxyl ions, so it is preferable to apply this method to reaction systems that do not contain ion-free ions. .
ところで、ここで付記寸べさこと4:11、−イオン交
換樹脂自体が触媒としては能Jる反応が多’/ d’−
+るということである。例λば、カチAン交換樹脂し1
、エステル、アセタール、7′ミドなどの生成や加水分
解、ニトリル、■ポキシへの水和(7との反応の触媒ど
なる。またアニオン交模樹11)jは、アルドール縮合
反応などの触媒として使用される。By the way, there are many reactions in which the ion exchange resin itself can act as a catalyst.
It means +. For example, for example, if the exchange resin is 1
, formation and hydrolysis of esters, acetals, 7' amides, etc., hydration to nitrile, ■ poxy (catalyst for reaction with 7. Also, anionic hybrid 11) j is used as a catalyst for aldol condensation reactions, etc. be done.
これに対して本発明にかかる内部9’、* 4I8電i
t!!代触媒のイオン交換樹脂(:1イAン伝導竹Iこ
tJをつかさどるものであるので、十)4(の如さ、イ
オン交換樹脂自体が触媒として機能するよう/、’r
(si、 ir汎、と区別ざるべきである。On the other hand, the internal 9′, *4I8 electric i according to the present invention
T! ! Ion exchange resin as a substitute catalyst (: 1) Since it is responsible for the conductive bamboo, 4 (as in, the ion exchange resin itself functions as a catalyst.)
(There should be a distinction between si and ir-pan.
一方、最近では、イオン交換樹脂に、金属Rに遷移金属
を担持させた触媒を用いて、ベンジル1勺ベンゾインの
還元を行%い1qることあろい1;に1−ロベンゼンの
還元によるアニリンの生成が可能という報告もある。On the other hand, recently, using a catalyst in which metal R supports a transition metal on an ion-exchange resin, reduction of benzyl 1 x benzoin has been carried out. There are also reports that it can be generated.
しかし、これらの従来の触[目よ、イオン交換樹脂自体
f)<、本発明のJ:うイ「水素イオンあるいは水酸(
Aンが伝脣する電解質としてで(1、なく、触媒どしで
1幾能しでいるし、さらには、本発明のJ、うに、電解
酸化に有効イr金属ど電解還元に右す1な金属を用いる
ことや、フッ素樹脂にJ:る反応物質の吸着リイトの適
正化という触fi Mu Fit思想がイ3′いなどの
爪味からしで、本発明の触媒ど(J、明らかに巽なった
ムのとみイ「7ベきである。However, these conventional catalysts [eyes, ion exchange resin itself f) <, J of the present invention
A acts as an electrolyte (1, not a catalyst), and furthermore, J of the present invention is effective for electrolytic oxidation, and is effective for electrolytic reduction of metals. The catalysts of the present invention (J, clearly Tatsumi Nata Mu no Tomii: ``It's 7-be.
双手、本発明の 実施例に゛ついて詳述する。An embodiment of the present invention will now be described in detail.
実施例
平均N(直径が20I!の白金ブラック粉末109ど平
均粒径が10 llの黒鉛化カーボンブラック20どス
チレン−ジビニルベンビン九重合体にスルフィン酸基を
導入してなる平均粒径がSftのイオン交換樹脂粉末5
gとをよく混合したしのに、蒸溜水を10m1加え、i
l+ (f J、(混合1ノだものに、固形分が60%
のポリ 4ノツ化1−ヂ1ノン水懸濁液を31111加
え、充分混練したちの4 日真空乾燥し、次いで直径が
3m…、良さが5ml1lのペレットをホットプレス法
、80℃で成形した。か<t、C内部短絡電池式触媒を
製作した。Examples: Platinum black powder 109 with an average diameter of 20 I!, graphitized carbon black 20 with an average particle diameter of 10 liters, and a sulfinic acid group introduced into a styrene-divinylbenvin nonapolymer with an average particle diameter of Sft. Ion exchange resin powder 5
Add 10ml of distilled water to the mixture well mixed with g,
l+ (f J, (mixture 1, solids content is 60%
Added 31111 of an aqueous suspension of polytetra-1-di-1-non, thoroughly kneaded, and vacuum-dried for 4 days. Then, pellets with a diameter of 3 m and a quality of 5 ml/l were molded at 80°C using a hot press method. . A <t, C internally shorted battery type catalyst was manufactured.
次にこの内部短絡電池式触媒べ1ノツトをメタノール1
01ど、水1001111からなる混合溶液中に入れ、
この混合溶液に室温C空気へ−吹き込/uだ。ぞの結果
1時間の後のホルムアルデヒドを分析し7たところ、メ
タノールから小11ノムノ’/し/!ヒlI\の酸化率
は54%であ−)た。Next, pour one knot of this internally shorted battery type catalyst into one part of methanol.
01, into a mixed solution consisting of water 1001111,
Blow air into this mixed solution at room temperature. As a result, formaldehyde was analyzed after 1 hour and it was found that it was mixed with methanol. The oxidation rate of HillI was 54%.
比較例
上記実施例において、イオン交1% +s・+脂を含ま
イ1い触媒により、同様の実験を行なったところ、メタ
ノールのホルムアルデヒドへの酸化率は7%(”あった
。Comparative Example When a similar experiment was carried out in the above example using a catalyst containing 1% ion exchange +s·+ fat, the oxidation rate of methanol to formaldehyde was 7%.
つまり、従来例では、単なる接触反応のために、メタノ
ールの酸化はあまり進まないのにス41)、本発明のよ
うに内部短絡電池式触媒を用いるとメタノールの酸化が
より進むことが瞭然としている。In other words, in the conventional example, the oxidation of methanol does not progress much due to a mere catalytic reaction (41), but it is clear that the oxidation of methanol progresses more when an internally shorted battery type catalyst is used as in the present invention. .
1ニ述の実施例では白金プラッタ粉末とイオン交換樹脂
との接触界面で、主として、メタノールの電解酸化反応
が起り、黒tit化カーボンブラックとイオン交換樹脂
との接触界面で、ill素の電解還元13−
が起り、白金ブラックと黒鉛化カーボンとの接触部で、
短絡電流が流、れる。In the example described in 1.2 above, the electrolytic oxidation reaction of methanol mainly occurs at the contact interface between the platinum platter powder and the ion exchange resin, and the electrolytic reduction of ill element occurs at the contact interface between the titified carbon black and the ion exchange resin. 13- occurs at the contact area between platinum black and graphitized carbon,
Short circuit current flows.
以」−訂)ホぜ゛る如(、本発明は有機化合物の酸化も
しくは還元をおこイ1つせるための全く新しい触媒段t
1思想にもとづく内t′JI′rI絡電池式触媒全提供
式触媒4−The present invention provides a completely new catalyst stage for the oxidation or reduction of organic compounds.
Based on the concept of t'JI'rI t'JI'rI tangled battery type catalyst all-provided type catalyst 4-
Claims (1)
体を電解酸化Jるのに右動イ1′電了伝導体粉末と(:
4ン伝導体とじてのイオン交換樹脂の粉末もl)くは知
繊屏1どの混合物をフッ素樹脂からなるれ1.省剤で結
石してなることを特徴とする有1幾化合物を酸化もしく
は還元するための内部短yIJ電池1(触媒。An electron conductor powder effective for electrolytically reducing an oxidant and an electron conductor powder effective for electrolytically oxidizing a reductant.
4. Ion exchange resin powder as a conductor can also be used as a fluororesin mixture. An internal short YIJ battery 1 (catalyst) for oxidizing or reducing a chemical compound characterized in that it is formed by concretions in a chemical-saving manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58151132A JPS6044044A (en) | 1983-08-18 | 1983-08-18 | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58151132A JPS6044044A (en) | 1983-08-18 | 1983-08-18 | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6044044A true JPS6044044A (en) | 1985-03-08 |
Family
ID=15512065
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58151132A Pending JPS6044044A (en) | 1983-08-18 | 1983-08-18 | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6044044A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5024272A (en) * | 1973-06-29 | 1975-03-15 | ||
JPS5074592A (en) * | 1973-10-29 | 1975-06-19 | ||
JPS57197032A (en) * | 1981-05-21 | 1982-12-03 | Bayer Ag | Method for carring out catalytic reaction in aqueous medium |
-
1983
- 1983-08-18 JP JP58151132A patent/JPS6044044A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5024272A (en) * | 1973-06-29 | 1975-03-15 | ||
JPS5074592A (en) * | 1973-10-29 | 1975-06-19 | ||
JPS57197032A (en) * | 1981-05-21 | 1982-12-03 | Bayer Ag | Method for carring out catalytic reaction in aqueous medium |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2020107539A1 (en) | Preparation method for catalyst for producing methyl methacrylate, and application thereof | |
JP2005526596A (en) | Method for fixing water-soluble nano-dispersed metal oxide colloids as they are | |
JP2005536829A (en) | Fuel additive for fuel cells | |
CN107398277A (en) | Application of the cupro-nickel molten iron talcs catalyst in wastewater containing phenol of degrading | |
CN108722420A (en) | A kind of preparation method of copper silicon systems catalyst | |
JPH06505668A (en) | Alloy catalyst production method | |
CN105749717B (en) | A kind of electrochemical treatments SO2Gas-diffusion electrode preparation method | |
JPH0581303B2 (en) | ||
CN111468120B (en) | CoFeNiO X Layered hollow nanocage electrocatalyst and preparation method and application thereof | |
JP2022512559A (en) | Modified CNF membrane capable of catalytic decomposition of 4-nitrophenol and its preparation method and application | |
CN109621951A (en) | A kind of three-way catalyst and preparation method thereof preparing glyceric acid for aoxidizing glycerol | |
CN104492453A (en) | Carbon supported Co3O4-Mn3O4 double metal oxide composite catalyst and preparation method thereof | |
JP3138732B2 (en) | Catalyst for oxygen electrode of integrated regeneration type polymer electrolyte fuel cell | |
JPS6044044A (en) | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound | |
CN106984326A (en) | A kind of PtPdAu/ loaded nanos magnetic catalyst and preparation method thereof | |
Singh et al. | Replacing Anodic Oxygen Evolution Reaction with Organic Oxidation: The Importance of Metal (Oxy) Hydroxide Formation as the Active Oxidation Catalyst | |
JP2003100308A (en) | Cathode electrode catalyst for fuel cell and method of manufacturing the same | |
CN108640824A (en) | A kind of method that catalysis oxidation benzyl alcohol prepares benzaldehyde | |
CN107185552A (en) | A kind of method that polynary metal oxide catalyst catalysis prepares resorcinol | |
JPS6044052A (en) | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound | |
JPS6044051A (en) | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound | |
JPS6044047A (en) | Internal shortcircuit battery type catalyst for oxidizing or reducing organic compound | |
CN115254188B (en) | Method for preparing amphiphilic composite catalyst Pd@IL/CNT-COOH by one-pot method | |
JPS6174649A (en) | Manufacture of catalyst | |
JPS6174648A (en) | Manufacture of catalyst |