TW322432B - - Google Patents
Download PDFInfo
- Publication number
- TW322432B TW322432B TW083104711A TW83104711A TW322432B TW 322432 B TW322432 B TW 322432B TW 083104711 A TW083104711 A TW 083104711A TW 83104711 A TW83104711 A TW 83104711A TW 322432 B TW322432 B TW 322432B
- Authority
- TW
- Taiwan
- Prior art keywords
- catalyst
- platinum
- activated carbon
- aqueous solution
- ministry
- Prior art date
Links
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 76
- 239000003054 catalyst Substances 0.000 claims description 67
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 62
- 229910052697 platinum Inorganic materials 0.000 claims description 37
- 150000003058 platinum compounds Chemical class 0.000 claims description 18
- 239000007864 aqueous solution Substances 0.000 claims description 15
- 239000000243 solution Substances 0.000 claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- 238000011049 filling Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 12
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 10
- 150000001875 compounds Chemical class 0.000 claims description 8
- 239000007900 aqueous suspension Substances 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 6
- 230000002829 reductive effect Effects 0.000 claims description 6
- 239000003638 chemical reducing agent Substances 0.000 claims description 5
- 239000002244 precipitate Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 239000003513 alkali Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- JOKPITBUODAHEN-UHFFFAOYSA-N sulfanylideneplatinum Chemical compound [Pt]=S JOKPITBUODAHEN-UHFFFAOYSA-N 0.000 claims 1
- 150000003671 uranium compounds Chemical class 0.000 claims 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 13
- 229910052717 sulfur Inorganic materials 0.000 description 13
- 239000011593 sulfur Substances 0.000 description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 230000000694 effects Effects 0.000 description 9
- 239000007800 oxidant agent Substances 0.000 description 9
- 239000000725 suspension Substances 0.000 description 9
- 239000002253 acid Substances 0.000 description 8
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- 238000004073 vulcanization Methods 0.000 description 7
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical group [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 6
- 229910052739 hydrogen Inorganic materials 0.000 description 6
- 239000001257 hydrogen Substances 0.000 description 6
- 238000005984 hydrogenation reaction Methods 0.000 description 6
- ATGUVEKSASEFFO-UHFFFAOYSA-N p-aminodiphenylamine Chemical compound C1=CC(N)=CC=C1NC1=CC=CC=C1 ATGUVEKSASEFFO-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- WBYWAXJHAXSJNI-VOTSOKGWSA-M .beta-Phenylacrylic acid Natural products [O-]C(=O)\C=C\C1=CC=CC=C1 WBYWAXJHAXSJNI-VOTSOKGWSA-M 0.000 description 3
- WBYWAXJHAXSJNI-SREVYHEPSA-N Cinnamic acid Chemical compound OC(=O)\C=C/C1=CC=CC=C1 WBYWAXJHAXSJNI-SREVYHEPSA-N 0.000 description 3
- 239000012018 catalyst precursor Substances 0.000 description 3
- 229930016911 cinnamic acid Natural products 0.000 description 3
- 235000013985 cinnamic acid Nutrition 0.000 description 3
- 150000004687 hexahydrates Chemical class 0.000 description 3
- WBYWAXJHAXSJNI-UHFFFAOYSA-N methyl p-hydroxycinnamate Natural products OC(=O)C=CC1=CC=CC=C1 WBYWAXJHAXSJNI-UHFFFAOYSA-N 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- LNTHITQWFMADLM-UHFFFAOYSA-N gallic acid Chemical compound OC(=O)C1=CC(O)=C(O)C(O)=C1 LNTHITQWFMADLM-UHFFFAOYSA-N 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- XMIIGOLPHOKFCH-UHFFFAOYSA-N 3-phenylpropionic acid Chemical compound OC(=O)CCC1=CC=CC=C1 XMIIGOLPHOKFCH-UHFFFAOYSA-N 0.000 description 1
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 description 1
- RSPISYXLHRIGJD-UHFFFAOYSA-N OOOO Chemical class OOOO RSPISYXLHRIGJD-UHFFFAOYSA-N 0.000 description 1
- 239000004280 Sodium formate Substances 0.000 description 1
- 239000005708 Sodium hypochlorite Substances 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- ZGSDJMADBJCNPN-UHFFFAOYSA-N [S-][NH3+] Chemical compound [S-][NH3+] ZGSDJMADBJCNPN-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229940045985 antineoplastic platinum compound Drugs 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000002079 cooperative effect Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- QLACLEPYLWLNTD-UHFFFAOYSA-N dihydrocinnamic acid Natural products COc1ccc(CCC(O)=O)c(O)c1OC QLACLEPYLWLNTD-UHFFFAOYSA-N 0.000 description 1
- VDQVEACBQKUUSU-UHFFFAOYSA-M disodium;sulfanide Chemical compound [Na+].[Na+].[SH-] VDQVEACBQKUUSU-UHFFFAOYSA-M 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000008098 formaldehyde solution Substances 0.000 description 1
- 229940074391 gallic acid Drugs 0.000 description 1
- 235000004515 gallic acid Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- RZDQHXVLPYMFLM-UHFFFAOYSA-N gold tantalum Chemical compound [Ta].[Ta].[Ta].[Au] RZDQHXVLPYMFLM-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- VLTRZXGMWDSKGL-UHFFFAOYSA-M perchlorate Inorganic materials [O-]Cl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-M 0.000 description 1
- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical compound OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 description 1
- JRKICGRDRMAZLK-UHFFFAOYSA-L peroxydisulfate Chemical compound [O-]S(=O)(=O)OOS([O-])(=O)=O JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000005932 reductive alkylation reaction Methods 0.000 description 1
- 239000012279 sodium borohydride Substances 0.000 description 1
- 229910000033 sodium borohydride Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 1
- 235000019254 sodium formate Nutrition 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
- B01J37/031—Precipitation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
- B01J23/42—Platinum
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/02—Sulfur, selenium or tellurium; Compounds thereof
- B01J27/04—Sulfides
- B01J27/043—Sulfides with iron group metals or platinum group metals
- B01J27/045—Platinum group metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/20—Sulfiding
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C209/00—Preparation of compounds containing amino groups bound to a carbon skeleton
- C07C209/24—Preparation of compounds containing amino groups bound to a carbon skeleton by reductive alkylation of ammonia, amines or compounds having groups reducible to amino groups, with carbonyl compounds
- C07C209/26—Preparation of compounds containing amino groups bound to a carbon skeleton by reductive alkylation of ammonia, amines or compounds having groups reducible to amino groups, with carbonyl compounds by reduction with hydrogen
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
- C07C51/36—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by hydrogenation of carbon-to-carbon unsaturated bonds
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
B7 五、發明説明(1 ) - 本發明係關於含鉑/活性碳之經硫化觸媒及其製備方 法0 含有贵金靥的經硫化觸媒已大量生產且使用了數十年 。供製備此類觸媒的方法記載於,例如,DE — P S 21 50 220中。利用將觸媒部分毒化,即 用含硫的化合物硫化含貴金屬的觸媒,可使觸媒對於所求 之化學反應具有較高的選擇性,但觸媒的活性通常會降低 。人們對於硫化機構本身,結合至觸媒表面之硫的本質或 是硫,贵金靥及載髋之間的關係,所知甚少。 就鹵化的硝基芳族化合物之選擇性氫化反應(參見, 例如,已公開之德國專利申請案 P 42 18 8 6 6. 0)以及還原性烷基化反應( DE — OS 27 36 228)而言,含有鉑爲貴金 屬且含有活性碳爲載體的觸媒較任何其它觸媒系統爲佳。 此等觸媒在這些反應中的選擇性可藉硫化進行部分毒 化,而獲改善。 經濟部中央標準局員工消費合作社印製 硫本身或其它含硫的化合物,諸如H2S ,二甲亞碩 ’ (NH4) 2S,Na2S,Na2S〇4等皆可作爲硫化 劑:其中,例如,硫可由含硫化合物,藉强酸之作用(例 如,H2S〇4)而釋出。在此情況下,濃度爲〇· 1至 1〇莫耳(硫)/莫耳(鉑),但較佳爲〇. 1至2莫耳 (硫)/莫耳(鉑)。 本發明之目標係在於提供此類的觸媒,及其製法:如 是觸媒在用習知之硫化劑予以硫化,而致部分毒化後,具 83. 3. 10,000 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) A7 _B7_ 五、發明説明(2 ) - 有較習知觸媒好很多的催化力。 以含有鉑/活性碳的硫化觸媒,可達本發明之目檩, 如是觸媒可由下列的方法製得:含鉑化合物的水溶液與活 性碳之水懸浮液混合:將所得之混合液加熱至7 0至 1 0 o°c之間的溫度:在相同之恆定溫度下,用鹸使鉑化 合物沈澱並角還原劑使幾乎不溶解的鉑化合物還原;濾出 並清洗依此方式所得的觸媒;用硫化劑處理該觸媒並再次 清最終的_觸媒;此方法的特徵在於:鉑化合物的水溶液含 有氧化劑。 最終觸媒中的鉑含量係在0 .1至5重量%之間(相 對於活性碳)。在將粉狀的活性碳載體浸漬於鉑化合物之 水溶液之前,先將氧化劑加至該水溶液,出人意料地,會 產生以習用硫化劑硫化後可具顯著改善催化力的含鉑相。 此外,亦令人霣驚的是,藉由添加氧化劑而製得之觸 媒,在硫化之前,並未眞正地呈現出改良之催化反應的能 力。 經濟部中央標準局員工消費合作社印製 I. i Ml J— 1^- ^ I n I I ^ * (請先閲讀背面之注意事項再填寫本頁) 適用之活性碳載體爲酸活性碳及有或無經後繽之酸洗 的蒸汽活性碳。諸如磷酸或硝酸之無機酸通常可用於酸活 化0 依活化之方法及原料之不同,可製出殘餘灰量爲1至 5重量%,pH大於4且平均粒徑在1 〇至4 0 之間 的活性碳。活性碳的比表面積非常高,通常在5 0 0至 1 5 0 Om2 /g之間。總孔隙度一般皆大於〇. 5m芡 / g 。 ^纸張尺渡逋用中國國家標準(CNS ) A4規格(210X297公釐) 83. 3. 10,000 經濟部中央標準局員工消費合作杜印製 A7 B7 五、發明説明(3 ) ~ 活性碳之PH値的測置方法如下:將1g活性碳懸浮 於1 0 OmJ?水中,在2 5°C下撹拌5分鐘後,即進行 p Η的測量。用於本發明觸媒的活性碳宜爲P Η大於5者 Ο 適用的氧化劑爲無機的過化合物(inorganic perco-mpounds ),諸如,過硫酸塩及過氯酸塩;次氯酸鈉以及 羥基過氧化烷類,但以H2〇2較佳。濃度爲0. 1至 10. 0莫耳/莫耳(鉑),以〇· 5至5· 〇莫耳/莫 耳(鉑)較佳。 適用的硫化劑爲可由先前技藝得知的所有硫化劑。 在將鉑化合物之水溶液與活性碳之水懸浮液混合時, 幾乎不溶的鉑化合物會部分沈澱在活性化合物上。加鹸至 含鉑溶液與活性碳懸浮液所形成的混合液中,使呈幾乎不 溶化合物形式的鉑沈澱完全。逋合的鹸爲碳酸鈉,氫氧化 鈉或氫氧化紳。 本發明之另一目的係提供製備硫化觸媒的方法,其包 含下列步驟:含鉑化合物的水溶液與活性碳之水懸浮液混 合:將所得之混‘液加熱至7 0至1 0 0°C之間的溫度; 在相同之恆定溫度下,用鹸使鉑化合物沈澱並用還原劑使 幾乎不溶解的鉑化合物還原:濾出並清洗依此方式所得的 觸媒:用硫化劑處理該觸媒並再次清洗最終的觸媒;此方 法的特徵在於:鉑化合物的水溶液含有氧化劑。宜將用完 全去離子水(D I水)或蒸餾水,來清洗觸媒。 活性碳之水懸浮液的濃度宜爲5至3 0重量%,各種 本張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83. 3.10,000 (請先閲讀背面之注意事項再填寫本頁) --訂 經濟部中央標準局貝工消費合作社印製 A7 S22432__ 五、發明説明(4 ) " 的水溶液鉑化合物皆可使用,六氯鉑酸六水合物已證實爲 特別佳者。 加至鉑溶液之氧化劑(宜爲過氧化氫)的置爲〇. 1 至10. 0莫耳/莫耳(鉑),宜爲〇· 5.至5. 0莫耳 /莫耳(鉑)。 活性碳懸浮液及鉑溶液係於搅拌的條件下,混合在一 起並加熱至7 0〜1 0 0°C,然後,藉由添加鹸(諸如碳 酸鈉或苛性蘇打溶液),令鉑以其幾乎不溶之化合物的形 式,沈澱在活性碳上;然後,在同一溫度下,予以還原, 道或許可藉添加諸如肼,甲酸鈉,硼氫化鈉或甲醛等還原 劑(宜爲甲醛)之助。 將鉑溶液及鹸添加至活性碳懸浮液的順序並不重要。 因此,鹸可在活性碳懸浮液導入鉑溶液之前,先加至活性 碳懸浮液中。 在濾出及清洗依此方式所得之P t /C觸媒後,可在 常溫下將硫化劑(例如,二甲亞碩或硫化氨)連同强酸( 如硫酸),一起加至觸媒水懸浮液中。 經硫化之觸媒應含有0.1至5. 0重量%之鉑,宜 爲〇· 5至3. 5重量%;硫的含量爲〇. 1至1. 〇莫 耳/莫耳(鉑),宜爲0· 1至2莫耳/莫耳(鉑)。 除了前述之施行方法外,亦可將行下列方法:將含有 氧化劑及鉑的溶液加至活性碳懸浮液,或是將活性碳加至 含氧化劑及銷的溶液,或是將含有氧化劑及軸的溶液噴灑 至活性碳上。 —1^ ΊI-^---ftT- -· (請先閱讀背面之注意事項再填寫本買) -訂 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83. 3. 10,000 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(5 ) - 爲了安定含鉑的溶液,將無機酸,如塩酸,硫酸或硝 酸加至該溶液中,有時會有所助益。 現以幾個實例,來說明本發明。寅例1係記述本發明 之觸媒及先前技藝之對照觸媒的製備。於低壓試驗中,硏 究並比較各種觸媒之非硫化前驅體的活性。於實例3中, 本發明之硫化觸媒於低壓試驗中,進行活性及選擇性的試 驗並與對照觸媒相比較。 實例1 :觸媒的製備 使用具有下列物化特性之活性碳,作爲所有觸媒的載 體. 原料: 粉狀活性碳 比表面積: 1,500m2/g (ASTM-D-3663) 總孔隙度: 1 . 5 m 1 / g (ASTM-D-4284) 平均粒徑: 22 μ m (ASTM-D-4464) pH : 10 灰置: <2 % A)製備觸媒前驅體(p t + H2〇2/C )(未硫化 ) 爲製備鉑含量爲3 %之觸媒,茲將9 7 g活性碳(乾 重)搅拌至蒸餾水中,搅拌速度爲3 0 0 r pm,將1 2 g 2 5%强度之六氯鉑酸六水合物的水溶液(相當於3 g 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83. 3.10,000 —•^1 I n I I n I ^In I n I T .^1 I I I It ^ ^i 「 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(6 ) - 釣)及3m又3 0%强度之Η 2〇2水溶液(相當於2莫耳 Η2〇2/莫耳(鉑))加至該懸浮液中。 然後,將懸浮液加熱至8 0 Ό並在持績搅拌的條件下 ,添加碳酸鈉,以沈澱析出幾乎不溶的氫氧化物。爲使沈 澱物還原,則添加1. 8m$37%强度的甲醛溶液。在 還原期間,將懸浮液之溫度保持在8 0X。還原完成後, 於吸濾器上,濾出觸媒並用DI水予以清洗。
B )製備本發明之硫化觸媒(P t + H2〇2+S/C ) 爲製備依本發明之鉑含量爲3 %的觸媒,先依A部分 所述者,製出觸媒,再依DE-PS21 50 220 之實例1 ,用二甲亞碩予以硫化。經硫化之觸媒的總硫含 量爲約0. 4莫耳硫/莫耳(鉑)。 藉由適當地增加硫化劑的量,可製得鉑含量相同但硫 量爲二或四倍的觸媒。 依與前述相同的程序,但同時增加六氯鉑酸六水合物 ,苛性蘇打溶液及硫化劑的量,可製得各種不同鉑含量的 觸媒。
C)製備對照觸媒:Pt/C 爲與本案之觸媒相比較,依與寅例1之A或B部分相 同的方式,但不添加H2〇2,製出載於碳上的含鉑觸媒。 (請先閱讀背面之注意事項再填寫本頁) 訂 本紙張尺度適用中國國家標準(CNS ) A4規格(21〇乂297公釐) 83. 3. 10,000 經濟部中央標準局員工消費合作社印製 A7 _B7_五、發明説明(7 ) - 實例2:觸媒前驅體(未硫化)的低壓試驗 於下列反應條件下,在肉桂酸的氫化反應中,測試觸 媒前驩髋的活性: 將2 0 Omg觸媒加至1 0 g肉桂酸(其係於1 2 0 m j?乙醇中)並轉置於攪拌反器中,將反應器裝配有鼓風 製備器,溫度計及氣入口。 首先,用大氣壓下的氮小心地漂沖反應器。然後,在 2 5 °C的反應溫度下,於反應器中,設定比大氣壓高1 0 毫巴的氫恒壓,並藉助鼓風搅拌器(2 0 0 Or pm), 將氫平均分散於溶液中。 肉桂酸氫化爲二氫肉桂酸之氫化反應中的催化活性被 用來測量催化力,且其係以mj?(氫)/ g (觸媒)/ m i η表示。用來計算該催化活性的反應時間係指導入氫 後,第三及第八分鐘之間反應時間。 表1所示之試驗結果乃依實例1之A部分或C部分所 製得之觸媒(未硫化)的結果。 (請先閱讀背面之注意事項再填寫本頁) -訂 本紙張尺度適用中ΐ國家ϋ ( CNS ) Α4規格(210X 297公釐) 83_ 3. 10,000 « - 10 - 322432 B7 五、發明説明(8 ) 催化活性 寅例 組成 ral H2/g 觸媒 /min 1C 3.0¾ Pt/C 2 4 5' (220-280) 1A (3.0¾ Pt + Η 2 0 2 ) / C 2 4 0 ' (230-270) 1C 1.0% Pt/C 95' (80-120) 1 A (1 . 0% Pt + Η 2 0 2 ) / C 90' (70-110) (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局舅工消費合作社印裝 •進行10個實驗之平均値。 表1顯示所有的觸媒前驅體皆具有同等的活性。 實例3 :觸媒(硫化後)的高壓試驗 於以甲基異丁基酮(MI BK)進行之對胺基二苯胺 (PADPA )的還原性氫化反應中,將實例1 B之本發 明觸媒的活性及選擇性與依實例1C之先前技藝的對照觸 媒之活性及選擇性作比較。 爲此一目的,茲將3. 77莫耳?八0卩八連同 4. 63 莫耳MIBK 及 1. 38g3%Pt/C 觸媒( 相當於0. 2重量%,參照PADPA的量)一起加至 2义的壓熱器中。將壓熱器密封,先後用氮及氫予以漂洗 ,並施予5 0巴的氫。在攪拌的條件下,將反應混合液加 熱至1 9 0°C。在6 0,9 0及1 2 0分鐘的反應時間點 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83.3. 10,000 « - 11 - A7 B7 五、發明説明(9 ) - ,取出樣品並加以分析。 表2顯示分析樣品中尙未轉化之P A D P A的殘量以 及使PAD PA之殘量降至2重量%所需之氫化時間。 (請先閲讀背面之注意事項.再填寫本頁) 、-° 經濟部中央標準局員工消費合作社印製 83. 3. 10,000 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -12 A7 B7 五、發明説明(1〇 表2 : 實例 高壓試驗 殘量PADPA ⑻ PADPA殘量〈2%時的 氫化時間 [分鐘] 60分鐘 90分鐘 120分鐘 1C (3.0 Pt+S) 7.5 3.8 2.0 120 1C有二倍的S 11.3 5.9 2.8 135 1B (3.0 Pt+H2〇2+S)C 3.6 1.8 1.0 86 1B有二倍的S 4.2 2.0 1.1 90 1B有四倍的S 10.8 5.7 2.8 130 1-1. In - -I —I— --- I - tjl 士-. I -- i -I - II I! . TV - · +14 、T (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局負工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 83. 3. 10,000 13 - A7 B7 ^22432 五、發明説明(11 ) - 表2顯示,使用依本發明實例1 B的觸媒可得改良活 性,其活性較先前技藝者(實例1 C)高出達3 5%。其 選擇性不受H2〇2處理的影響。 (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 本紙張尺度適用中國國家標準(CNS ) A4規格(210父297公嫠) 83. 3. 10,000 ί 14
Claims (1)
- 322432 欲 A8 B8 C8 D8 ¥ I 六、申請專利範圍 附件二A : 第831Q4711號專利申請案 中文申請專利範圍修正本 (請先閱讀背面之注意事項再填寫本X ) 民_ 84年12月修正 1 .—種被負載於活性碳上之經硫化鉑觸媒,其可由 下列方法製得:令鈾化合物的水溶液與活性碳之水懸浮液 混合;將所得之混合液加熱至7 0至1 0 0°C之間的溫度 ;在相同之恆定溫度下,用鹼使鉑化合物沈澱並用還原劑 使幾乎不溶解的鉑化合物還原;濾出並清洗依此方式所得 的觸媒;用硫化劑處理該觸媒並再次清洗最終的觸媒; 其特徵在於:鉑化合物的水溶液含有過氧化氫,其量 對每莫耳鉑而言爲0.1至10.0莫耳。 2 .如申請專利範圍第1項之經硫化觸媒,其中舶化 合物的水溶液中,過氧化氫之量對每莫耳鉑而言爲0 . 5 至5 · 0莫耳。 ' 3' .二種製備如申請專利範圍第1項之被負載於栝性 經濟部中央標準局負工消費合作社印裝 碳上之經硫化舶觸媒的方法,其包括下列步驟:令鉑化合 物的水溶液與活性碳之水懸浮液混合;將所得之混合液加 熱至7 0至1 〇 〇°C之間的溫度;在相同之恆定溫度下, 用鹸使鉑化合物沈澱並用還原劑使幾乎不溶解的鉑化合物 還原;濾出並清洗依此方式所得的觸媒;用硫化劑處理該 觸媒並再次清洗最終的觸媒; 其特徵在於:鉑化合物的水溶液含有過氧化氫,其量 對每莫耳鉑而言爲〇 . 1至10 . 0莫耳。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 1 A8 B8 C8 D8 六、申請專利範圍4 .如申請專利範圍第3項之方法,其中過氧化氫之 量對每莫耳鉑而言爲0. 5至5. 0莫耳。 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標牟局員工消费合作社印製 本紙張尺度通用中國國家標準(CNS ) A4規格(210Χ297公釐) 2
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19934319648 DE4319648C2 (de) | 1993-06-14 | 1993-06-14 | Platin auf Aktivkohle enthaltender sulfidierter Katalysator |
| DE19944414491 DE4414491C1 (de) | 1994-04-26 | 1994-04-26 | Platin auf Aktivkohle enthaltender sulfidierter Katalysator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| TW322432B true TW322432B (zh) | 1997-12-11 |
Family
ID=25926752
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW083104711A TW322432B (zh) | 1993-06-14 | 1994-05-24 |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US5498585A (zh) |
| EP (1) | EP0629439B1 (zh) |
| JP (1) | JPH07148431A (zh) |
| KR (1) | KR950000217A (zh) |
| BR (1) | BR9402390A (zh) |
| CA (1) | CA2125800C (zh) |
| DE (1) | DE59401687D1 (zh) |
| TW (1) | TW322432B (zh) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5496789A (en) * | 1994-04-07 | 1996-03-05 | Basf Aktiengesellschaft | Hydrogenation catalyst based on a platinum metal partially poisoned with finely divided sulfur |
| DE19614153A1 (de) * | 1996-04-10 | 1997-10-16 | Basf Ag | Verfahren zur Herstellung eines Hydrierungskatalysators |
| US6013371A (en) * | 1997-11-20 | 2000-01-11 | Motorcarbon Llc | Carbon artifacts and compositions and processes for their manufacture |
| ITRM20020087A1 (it) * | 2002-02-20 | 2002-05-21 | Francesco Massimo De | Catalizzatori di metalli nobili e non e loro leghe per pile a combustibile ottenuti mediante trattamento termico a bassa temperatura. |
| CN1310704C (zh) * | 2003-12-24 | 2007-04-18 | 中国石油化工股份有限公司 | 一种耐硫脱氧催化剂及其制备方法和应用 |
| CN1327955C (zh) * | 2004-10-27 | 2007-07-25 | 中国石油化工股份有限公司 | 硫化铂脱氧催化剂的制备方法 |
| US7964695B2 (en) * | 2005-03-28 | 2011-06-21 | Albemarle Corporation | Chain extenders |
| CN101160283A (zh) * | 2005-03-28 | 2008-04-09 | 雅宝公司 | 二亚胺和仲二胺 |
| US8076518B2 (en) | 2005-03-28 | 2011-12-13 | Albemarle Corporation | Chain extenders |
| CN101351440A (zh) * | 2005-12-30 | 2009-01-21 | 雅宝公司 | 具有降低颜色的二胺 |
| EP2102265A1 (en) * | 2007-01-10 | 2009-09-23 | Albermarle Corporation | Formulations for reaction injection molding and for spray systems |
| KR20170034255A (ko) | 2015-09-18 | 2017-03-28 | 대구대학교 산학협력단 | 비대칭 코어-쉘 나노입자 구조에 기반한 산소환원용 전극촉매 및 그 제조방법 |
| KR102183156B1 (ko) | 2018-06-22 | 2020-11-25 | 대구대학교 산학협력단 | 비대칭 코어-쉘 나노입자 구조에 기반한 산소환원용 전극촉매 및 그 제조방법 |
| CN114931946A (zh) * | 2022-07-04 | 2022-08-23 | 上海大学 | 一种Pt/C复合催化剂及其制备方法和应用 |
Family Cites Families (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3138560A (en) * | 1959-12-17 | 1964-06-23 | Engelhard Ind Inc | Process for producing palladium on carbon catalysts |
| BE789749A (fr) * | 1971-10-08 | 1973-02-01 | Degussa | Procede pour la preparation d'un catalyseur contenant un metal noble supporte sur charbon actif pour l'hydrogenation selective de composes chloronitroaromatiques et catalyseur obtenu |
| FR2169464A5 (zh) * | 1972-01-26 | 1973-09-07 | Matra Engins | |
| NL7502968A (nl) * | 1975-03-13 | 1976-09-15 | Stamicarbon | Werkwijze voor het bereiden van edelmetaal- katalysatoren. |
| ZA774380B (en) * | 1976-08-13 | 1978-06-28 | Uniroyal Inc | Reduction and reductive alkylation of p-nitrosoarylamines with platinum metal sulfide catalysts |
| US4136059A (en) * | 1977-12-12 | 1979-01-23 | United Technologies Corporation | Method for producing highly dispersed catalytic platinum |
| JPS6348761A (ja) * | 1986-08-14 | 1988-03-01 | Fuji Electric Co Ltd | 燐酸型燃料電池のアノ−ド触媒の調製方法 |
| DE3713733A1 (de) * | 1987-04-24 | 1988-11-17 | Basf Ag | Verfahren zur herstellung von hydroxylammoniumsalzen |
| DE4022851A1 (de) * | 1990-07-18 | 1992-01-23 | Basf Ag | Platin-graphittraeger-katalysatoren und deren verwendung |
| DE4022853A1 (de) * | 1990-07-18 | 1992-01-23 | Basf Ag | Platin-graphittraeger-katalysatoren und deren verwendung |
-
1994
- 1994-05-24 TW TW083104711A patent/TW322432B/zh active
- 1994-06-10 EP EP94108930A patent/EP0629439B1/de not_active Expired - Lifetime
- 1994-06-10 DE DE59401687T patent/DE59401687D1/de not_active Expired - Fee Related
- 1994-06-13 US US08/259,677 patent/US5498585A/en not_active Expired - Fee Related
- 1994-06-13 BR BR9402390A patent/BR9402390A/pt not_active Application Discontinuation
- 1994-06-13 KR KR1019940013221A patent/KR950000217A/ko not_active Withdrawn
- 1994-06-14 CA CA002125800A patent/CA2125800C/en not_active Expired - Fee Related
- 1994-06-14 JP JP6132217A patent/JPH07148431A/ja active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| EP0629439A1 (de) | 1994-12-21 |
| CA2125800A1 (en) | 1994-12-15 |
| DE59401687D1 (de) | 1997-03-13 |
| KR950000217A (ko) | 1995-01-03 |
| JPH07148431A (ja) | 1995-06-13 |
| EP0629439B1 (de) | 1997-01-29 |
| US5498585A (en) | 1996-03-12 |
| BR9402390A (pt) | 1995-01-17 |
| CA2125800C (en) | 1999-02-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| TW322432B (zh) | ||
| CA2125781C (en) | Vinyl acetate catalyst preparation method | |
| Menuel et al. | Cyclodextrins as effective additives in AuNP-catalyzed reduction of nitrobenzene derivatives in a ball-mill | |
| Massaro et al. | Gold nanoparticles stabilized by modified halloysite nanotubes for catalytic applications | |
| US5449655A (en) | Process for preparing hydrogenation catalysts which contain noble metals on activated carbon | |
| GB2370795A (en) | A process for removing pyrophoric catalyst | |
| GB1069416A (en) | Improvements in or relating to the manufacture of catalysts | |
| KR940006404B1 (ko) | 수처리용 촉매 | |
| US3929891A (en) | Reduction of halonitroaromates using sulfited platinum on carbon catalysts | |
| TW294610B (zh) | ||
| CA1044215A (en) | Process for preparing catalysts containing platinum metal | |
| US4659683A (en) | Regeneration of inactive and poisoned platinum catalysts | |
| US3131156A (en) | Preparation of a silica-alumina cracking catalyst | |
| JPH10137587A (ja) | 担持貴金属触媒の製造方法 | |
| JPH01135842A (ja) | 光触媒固定膜 | |
| Herrero et al. | Preparation of rhodium–phyllosilicate catalysts without leaching in liquid‐phase 1‐hexene hydrogenation | |
| CN108821354A (zh) | 一种制备硝酸铱溶液的方法 | |
| JPH01159056A (ja) | ヒドロキシルアンモニウム塩の製造法およびその触媒 | |
| WO2000058243A1 (fr) | Procede de traitement de matieres premieres organiques et catalyseur permettant de mettre en oeuvre ce procede | |
| Kralik et al. | Deactivation of palladium catalysts supported on functionalised resins in the reduction of aromatic nitrocompounds | |
| JP2595582B2 (ja) | ルテニウム含有触媒の製造法 | |
| TW438754B (en) | Preparation of phenol or phenol derivatives | |
| JP3244605B2 (ja) | 粒度調整された貴金属炭素触媒 | |
| US2429971A (en) | Method of preparing a therapeutic zinc peroxide composition | |
| JP2003155301A (ja) | ヒドロキシエチルセルロースの製造方法 |