EA201171319A1 - Полиметаллический катализатор гидроконверсии и способ его получения - Google Patents
Полиметаллический катализатор гидроконверсии и способ его полученияInfo
- Publication number
- EA201171319A1 EA201171319A1 EA201171319A EA201171319A EA201171319A1 EA 201171319 A1 EA201171319 A1 EA 201171319A1 EA 201171319 A EA201171319 A EA 201171319A EA 201171319 A EA201171319 A EA 201171319A EA 201171319 A1 EA201171319 A1 EA 201171319A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- catalyst
- range
- catalyst precursor
- volumetric shrinkage
- sulfiding
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title abstract 5
- 239000012018 catalyst precursor Substances 0.000 abstract 4
- 239000011148 porous material Substances 0.000 abstract 3
- -1 VIB metal compound Chemical class 0.000 abstract 1
- 238000009835 boiling Methods 0.000 abstract 1
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 239000003085 diluting agent Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 150000002736 metal compounds Chemical class 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F15/00—Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table
- C07F15/04—Nickel compounds
- C07F15/045—Nickel compounds without a metal-carbon linkage
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- 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
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
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- 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
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
- B01J23/8885—Tungsten containing also molybdenum
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- 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
- B01J37/0018—Addition of a binding agent or of material, later completely removed among others as result of heat treatment, leaching or washing,(e.g. forming of pores; protective layer, desintegrating by heat)
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- 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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G49/00—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00
- C10G49/02—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used
- C10G49/04—Treatment of hydrocarbon oils, in the presence of hydrogen or hydrogen-generating compounds, not provided for in a single one of groups C10G45/02, C10G45/32, C10G45/44, C10G45/58 or C10G47/00 characterised by the catalyst used containing nickel, cobalt, chromium, molybdenum, or tungsten metals, or compounds thereof
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- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
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- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/613—10-100 m2/g
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- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
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- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/63—Pore volume
- B01J35/633—Pore volume less than 0.5 ml/g
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- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
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- 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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/107—Atmospheric residues having a boiling point of at least about 538 °C
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/30—Physical properties of feedstocks or products
- C10G2300/301—Boiling range
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Catalysts (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Предложены катализатор с низкой объемной усадкой и способ получения стойкого катализатора с низкой объемной усадкой. Катализатор получают сульфидированием предшественника катализатора, содержащего по меньшей мере одно соединение металла группы VIB; по меньшей мере одно соединение металла-промотора, выбранное из групп VIII, IIB, IIA, IVA и их сочетаний и имеющее степень окисления либо +2, либо +4; возможно, по меньшей мере один лигандообразующий агент; возможно, по меньшей мере, один разбавитель. В одном примере осуществления предшественник катализатора сначала подвергают формованию, а затем термической обработке до температуры в диапазоне от 50 до 200°С в течение времени от 15 мин до 12 ч, причем предшественник катализатора имеет низкую (менее 12%) объемную усадку после нагревания до температуры не менее 100°С в течение по меньшей мере 30 мин, например, при сульфидировании или в реакторе гидроочистки. В одном примере осуществления предшественник катализатора имеет мономодальное распределение по объему пор, по меньшей мере 90% пор являются макропорами, и суммарный объем пор составляет не менее 0,08 г/см. В другом примере осуществления катализатор пригоден для гидроочистки тяжелого дистиллята, имеющего температуру кипения в диапазоне от 343 до 454°С, средний молекулярный вес Mn в диапазоне от 300 до 400 и средний молекулярный диаметр в диапазоне от 0,9 до 1,7 нм.
Applications Claiming Priority (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US12/432,721 US7964525B2 (en) | 2009-04-29 | 2009-04-29 | Hydroconversion multi-metallic catalyst and method for making thereof |
US12/432,727 US8058203B2 (en) | 2009-04-29 | 2009-04-29 | Hydroconversion multi-metallic catalyst and method for making thereof |
US12/432,728 US7964526B2 (en) | 2009-04-29 | 2009-04-29 | Hydroconversion multi-metallic catalyst and method for making thereof |
US12/432,730 US8080492B2 (en) | 2009-04-29 | 2009-04-29 | Hydroconversion multi-metallic catalyst and method for making thereof |
US12/432,719 US7964524B2 (en) | 2009-04-29 | 2009-04-29 | Hydroconversion multi-metallic catalyst and method for making thereof |
US12/432,723 US7931799B2 (en) | 2009-04-29 | 2009-04-29 | Hydroconversion multi-metallic catalyst and method for making thereof |
PCT/US2010/030326 WO2010126689A2 (en) | 2009-04-29 | 2010-04-08 | Hydroconversion multi-metallic catalyst and method for making thereof |
Publications (2)
Publication Number | Publication Date |
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EA201171319A1 true EA201171319A1 (ru) | 2012-04-30 |
EA021708B1 EA021708B1 (ru) | 2015-08-31 |
Family
ID=43032741
Family Applications (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA201171319A EA021708B1 (ru) | 2009-04-29 | 2010-04-08 | Полиметаллический катализатор гидроконверсии и способ его получения |
EA201171320A EA020644B1 (ru) | 2009-04-29 | 2010-04-08 | Полиметаллический катализатор для гидропереработки и способ его получения |
EA201171321A EA020199B1 (ru) | 2009-04-29 | 2010-04-08 | Полиметаллический катализатор гидроконверсии и способ его получения |
Family Applications After (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA201171320A EA020644B1 (ru) | 2009-04-29 | 2010-04-08 | Полиметаллический катализатор для гидропереработки и способ его получения |
EA201171321A EA020199B1 (ru) | 2009-04-29 | 2010-04-08 | Полиметаллический катализатор гидроконверсии и способ его получения |
Country Status (9)
Country | Link |
---|---|
EP (3) | EP2424663B1 (ru) |
JP (3) | JP5759452B2 (ru) |
KR (2) | KR101722491B1 (ru) |
CN (3) | CN102413932B (ru) |
AU (3) | AU2010241966B2 (ru) |
CA (3) | CA2760413C (ru) |
EA (3) | EA021708B1 (ru) |
SG (3) | SG175405A1 (ru) |
WO (3) | WO2010126690A2 (ru) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017106125A1 (en) * | 2015-12-15 | 2017-06-22 | Uop Llc | Crystalline bis-ammonia transition metal molybdotungstate |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EA021708B1 (ru) * | 2009-04-29 | 2015-08-31 | Шеврон Ю.Эс.Эй. Инк. | Полиметаллический катализатор гидроконверсии и способ его получения |
AU2011326682B2 (en) * | 2010-11-11 | 2016-07-14 | Chevron U.S.A. Inc. | Hydroconversion multi-metallic catalyst and method for making thereof |
EP2654948A4 (en) * | 2010-12-20 | 2015-02-11 | Chevron Usa Inc | HYDROPROCESSING CATALYSTS AND MANUFACTURING METHOD THEREFOR |
JP6097224B2 (ja) * | 2010-12-30 | 2017-03-15 | シェブロン ユー.エス.エー. インコーポレイテッド | 水素化処理触媒を作製するための方法 |
US10400181B2 (en) * | 2015-12-15 | 2019-09-03 | Uop Llc | Crystalline bis-ammonia metal molybdate |
US10233398B2 (en) * | 2015-12-15 | 2019-03-19 | Uop Llc | Crystalline transition metal oxy-hydroxide molybdotungstate |
IT201600077340A1 (it) * | 2016-07-22 | 2018-01-22 | Eni Spa | Catalizzatori di idrotrattamento e procedimento di preparazione di detti catalizzatori. |
US9919987B1 (en) * | 2016-11-22 | 2018-03-20 | Chevron U.S.A. Inc. | Naphthene ring opening over self-supported multi-metallic catalysts |
FR3058909B1 (fr) * | 2016-11-24 | 2018-11-16 | Arkema France | Sels d'acide sulfonique pour la preparation de catalyseur metallique |
JP6924288B2 (ja) | 2017-10-18 | 2021-08-25 | ヒンドゥスタン ペトロリアム コーポレーション リミテッド | 重油のアップグレード用触媒 |
US10995013B2 (en) * | 2017-12-20 | 2021-05-04 | Uop Llc | Mixed transition metal tungstate |
US11033883B2 (en) * | 2018-06-26 | 2021-06-15 | Uop Llc | Transition metal molybdotungstate material |
US10737249B2 (en) * | 2018-06-26 | 2020-08-11 | Uop Llc | Crystalline transition metal molybdotungstate |
CN109759087B (zh) * | 2019-01-16 | 2022-02-08 | 安徽大学 | 一种NiS/MgAl-LDH光催化剂及其制备方法和应用 |
CN109985639A (zh) * | 2019-04-17 | 2019-07-09 | 河南师范大学 | 一种用原位构建的Pt/ZnS-rGO光催化剂及其制备氢气的方法 |
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US5841013A (en) | 1994-05-17 | 1998-11-24 | Exxon Research And Engineering Company | Aromatics hydrogenation with a new class of metal oxides |
US5866501A (en) * | 1996-02-23 | 1999-02-02 | Pradhan; Vivek R. | Dispersed anion-modified iron oxide catalysts for hydroconversion processes |
US6030915A (en) | 1996-03-11 | 2000-02-29 | Akzo Nobel N.V. | Process for preparing a large pore hydroprocessing catalyst |
US7288182B1 (en) * | 1997-07-15 | 2007-10-30 | Exxonmobil Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts |
US6162350A (en) * | 1997-07-15 | 2000-12-19 | Exxon Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
US6156695A (en) | 1997-07-15 | 2000-12-05 | Exxon Research And Engineering Company | Nickel molybdotungstate hydrotreating catalysts |
FR2775200B1 (fr) * | 1998-02-20 | 2000-04-28 | Inst Francais Du Petrole | Catalyseur comprenant une zeolithe nu-88, un element du groupe vb et son utilisation en hydroconversion de charges petrolieres hydrocarbonees |
CN1309476C (zh) * | 1999-01-15 | 2007-04-11 | 阿尔伯麦尔荷兰公司 | 新型混合金属催化剂及其用途 |
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FR2874837B1 (fr) * | 2004-09-08 | 2007-02-23 | Inst Francais Du Petrole | Catalyseur dope et procede ameliore de traitement de charges hydrocarbonees |
EP1791639A1 (en) * | 2004-09-22 | 2007-06-06 | Exxonmobil Research And Engineering Company | BULK Ni-Mo-W CATALYSTS MADE FROM PRECURSORS CONTAINING AN ORGANIC AGENT |
ES2511771T3 (es) * | 2005-10-26 | 2014-10-23 | Albemarle Netherlands B.V. | Catalizador para hidroprocesamiento a granel que comprende un metal del grupo VIII y el metal del grupo VIB molibdeno |
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US7951746B2 (en) * | 2006-10-11 | 2011-05-31 | Exxonmobil Research And Engineering Company | Bulk group VIII/group VIB metal catalysts and method of preparing same |
AU2008318836B2 (en) | 2007-10-31 | 2013-04-04 | Chevron U.S.A. Inc. | Hydroconversion processes employing multi-metallic catalysts and method for making thereof |
CA2703137C (en) * | 2007-10-31 | 2016-05-24 | Chevron U.S.A. Inc. | Hydroprocessing bulk catalyst and uses thereof |
EA021708B1 (ru) * | 2009-04-29 | 2015-08-31 | Шеврон Ю.Эс.Эй. Инк. | Полиметаллический катализатор гидроконверсии и способ его получения |
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2010
- 2010-04-08 EA EA201171319A patent/EA021708B1/ru not_active IP Right Cessation
- 2010-04-08 CA CA2760413A patent/CA2760413C/en active Active
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2017106125A1 (en) * | 2015-12-15 | 2017-06-22 | Uop Llc | Crystalline bis-ammonia transition metal molybdotungstate |
RU2699797C1 (ru) * | 2015-12-15 | 2019-09-11 | Юоп Ллк | Кристаллический бис-аммиачный молибдовольфрамат переходного металла |
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