Настройки

Укажите год
-

Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

Подробнее
-

Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

Подробнее

Форма поиска

Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Ведите корректный номера.
Укажите год
Укажите год

Применить Всего найдено 98. Отображено 98.
24-11-2016 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20160340272A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185.-. (canceled)86. A method for the preparation of ethane , ethylene or combinations thereof , the method comprising contacting a catalyst with a gas comprising methane , the catalyst comprising:{'sub': 4-x', 'x', '6, 'the formula Ln1Ln2O, wherein Ln1 and Ln2 are each independently a different lanthanide element, and x is a number ranging from greater than 0 to less than 4; and'}at least one doping element from one of groups 1-16, lanthanides, actinides or combinations thereof,{'sub': '2', 'wherein the catalyst further comprises a Cselectivity of greater than 50% and a methane conversion of greater than 10% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 700° C. or less.'}87. The method of claim 86 , wherein the at least one doping element is selected from groups 1-4 claim 86 , 8 claim 86 , 13 claim 86 , 14 claim 86 , lanthanides claim 86 , actinides and combinations thereof.88. The method of claim 86 , wherein the at least one doping element is selected from groups 1-6 claim 86 , 8 claim 86 , 11 claim 86 , 13-15 claim 86 , lanthanides claim 86 , actinides and combinations thereof.89. The method of claim 86 , wherein the at least one doping element is a rare earth element.90. The method of claim 86 , wherein the at least one doping element is Na claim 86 , Mg claim 86 , Ca claim 86 , Sr claim 86 , Ga claim 86 , Sc claim 86 , Y claim 86 , Zr claim 86 , In claim 86 , Nd claim 86 , Eu claim 86 , Sm claim 86 , Ce claim 86 , Gd claim 86 , Hf claim 86 , Ho claim 86 , Tm claim 86 , W claim 86 , La claim 86 , K claim 86 , Dy claim 86 , In claim 86 , Cs claim 86 , S claim 86 , Zn claim 86 , Rb ...

Подробнее
05-09-2017 дата публикации

Catalysts for natural gas processes

Номер: US0009751079B2
Принадлежит: Silura Technologies, Inc., SILURA TECH INC

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
22-08-2017 дата публикации

Catalysts for petrochemical catalysis

Номер: US0009738571B2

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
20-09-2016 дата публикации

Catalysts for petrochemical catalysis

Номер: US0009446387B2

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
24-01-2013 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20130023709A1
Принадлежит: SILURIA TECHNOLOGIES, INC.

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst comprising a mixed oxide of magnesium and manganese , wherein the catalyst further comprises lithium and boron dopants and at least one doping element from groups 4 , 9 , 12 , 13 or combinations thereof , wherein the catalyst comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.29-. (canceled)10. A catalyst comprising an oxide of a rare earth element , wherein the catalyst further comprises at least one doping element from groups 1-16 , lanthanides , actinides or combinations thereof , wherein the catalyst comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogenous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.11. The catalyst of claim 10 , wherein the at least one doping element is selected from groups 1-4 claim 10 , 8 claim 10 , 13 claim 10 , 14 claim 10 , lactinides claim 10 , actinides and combinations thereof.12. The catalyst of claim 10 , wherein the at least one doping element is selected from groups 1-6 claim 10 , 8 claim 10 , 11 claim 10 , 13-15 claim 10 , lactinides claim 10 , actinides and combinations thereof.13. The catalyst of claim 10 , wherein the at least one doping element is a rare earth element.14. The catalyst of claim 10 , wherein the at least one doping element is Na claim 10 , Mg claim 10 , Ca claim 10 , Sr claim 10 , Ga claim 10 , Sc claim 10 , Y claim 10 , Zr claim 10 , In claim 10 , Nd claim 10 , Eu claim 10 , Sm claim 10 , Ce claim 10 , ...

Подробнее
20-06-2013 дата публикации

POLYMER TEMPLATED NANOWIRE CATALYSTS

Номер: US20130158322A1
Принадлежит: SILURIA TECHNOLOGIES, INC.

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are prepared by polymer templated methods and are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to ethane and/or ethylene. Related methods for use and manufacture of the same are also disclosed. 1. A method for preparing a nanowire comprising a metal oxide , a metal oxy-hydroxide , a metal oxycarbonate or a metal carbonate , the method comprising:a) providing a solution comprising a plurality of polymer templates;{'sub': m', 'n', 'p, '(b) introducing at least one metal ion and at least one anion to the solution under conditions and for a time sufficient to allow for nucleation and growth of a nanowire comprising a plurality of metal salts (MXZ) on the template; and'}{'sub': m', 'n', 'p', 'x', 'y', 'x', 'y', 'z', 'x', 'y', '3', 'z', 'x', '3', 'y, '(c) optionally converting the nanowire (MXZ) to a metal oxide nanowire comprising a plurality of metal oxides (MO), metal oxy-hydroxides (MOOH), metal oxycarbonates (MO(CO)), metal carbonate (M(CO)) or combinations thereof'}wherein:M is, at each occurrence, independently a metal element from any of Groups 1 through 7, lanthanides or actinides;X is, at each occurrence, independently hydroxide, carbonate, bicarbonate, phosphate, hydrogenphosphate, dihydrogenphosphate, sulfate, nitrate or oxalate;Z is O;n, m, x and y are each independently a number from 1 to 100; andp is a number from 0 to 100.2. The method of claim 1 , wherein the polymer template comprises PVP (polyvinlpyrrolidone) claim 1 , PVA (polyvinylalcohol) claim 1 , PEI (polyethyleneimine) claim 1 , PEG (polyethyleneglycol) claim 1 , polyethers claim 1 , polyesters claim 1 , polyamides claim 1 , dextran claim 1 , sugar polymers claim 1 , functionalized hydrocarbon polymers claim 1 , functionalized polystyrene claim 1 , polylactic acid claim 1 , polycaprolactone claim 1 , polyglycolic acid claim 1 , poly(ethylene glycol)-polypropylene glycol)- ...

Подробнее
27-06-2013 дата публикации

NANOWIRE CATALYSTS AND METHODS FOR THEIR USE AND PREPARATION

Номер: US20130165728A1
Принадлежит: SILURIA TECHNOLOGIES, INC.

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 1. A catalytic nanowire comprising a combination of at least four different doping elements , wherein the doping elements are selected from a metal element , a semi-metal element and a non-metal element.2. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises a metal oxide.3. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises a lanthanide metal.4. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises LaO claim 1 , NdO claim 1 , YbO claim 1 , EuO claim 1 , SmO claim 1 , YO claim 1 , CeO claim 1 , PrOor combinations thereof.5. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises Ln1Ln2O claim 1 , wherein Ln1 and Ln2 are each independently a lanthanide element claim 1 , wherein Ln1 and Ln2 are not the same and x is a number ranging from greater than 0 to less than 4.6. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises LaNdO claim 1 , wherein x is a number ranging from greater than 0 to less than 4.7. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises LaNdO claim 1 , LaNdO claim 1 , LaNdO claim 1 , LaNdO claim 1 , LaNdO claim 1 , LaNdO claim 1 , LaNdOor combinations thereof.8. The catalytic nanowire of claim 1 , wherein the catalytic nanowire comprises a lanthanide oxide.9. The catalytic nanowire of claim 8 , wherein the lanthanide oxide comprises a mixed oxide.10. The catalytic nanowire of claim 9 , wherein the mixed oxide comprises Y—La claim 9 , Z—La claim 9 , P—La claim 9 , Ce—La or combinations thereof.11. The catalytic nanowire of claim 1 , wherein the doping elements are selected from Eu claim 1 , Na claim 1 , Sr claim 1 , Ca claim 1 , Mg claim 1 , Sm ...

Подробнее
10-01-2019 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20190010096A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogeneous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)86. A method for the oxidative coupling of methane , the method comprising contacting methane with a catalyst at temperatures ranging from about 550° C. to about 750° C. , wherein the method comprises a methane conversion of greater than 20% and a C2 selectivity of greater than 50% , and wherein the catalyst comprises the following formula:{'br': None, 'sub': x', 'y', 'z, 'ABO;'} A is an element from the lanthanides or group 2, 3, 4, 6 or 13;', 'B is an element from groups 4, 12 or 13 of the periodic table or Ce, Pr, Nd, Sm, Eu, Gd, Tb or Ho;', 'O is an oxygen anion; and', 'x, y and z are each independently numbers greater than 0,, 'whereinthe catalyst further comprising one or more dopants from any one of groups 2, 3 or the lanthanides, and provided that A and B are not the same.87. The method of claim 86 , wherein A is Ba claim 86 , Zr claim 86 , Sr claim 86 , Sm claim 86 , Hf claim 86 , Gd claim 86 , Er claim 86 , Y claim 86 , Ca claim 86 , La claim 86 , Mg claim 86 , W claim 86 , B claim 86 , Tb or Ce.88. The method of claim 86 , wherein B is Zn claim 86 , Hf claim 86 , Zr claim 86 , Al claim 86 , Ti claim 86 , Pr claim 86 , Nd claim 86 , Ce claim 86 , Sm claim 86 , Eu claim 86 , Gd claim 86 , Tb or Ho.89. The method of claim 86 , wherein A is from group 2 claim 86 , and B is from group 4.90. The method of claim 86 , wherein A is Ba claim 86 , Sr or Ca.91. The method of claim 86 , wherein B is Ti claim 86 , Zr or Hf.92. The method of claim 86 , wherein the catalyst has the formula ABO.93. The method of claim 86 , wherein the catalyst comprises one or more dopant from group 2.94. The method of claim 86 , wherein the catalyst comprises ...

Подробнее
16-01-2020 дата публикации

CATALYSTS FOR NATURAL GAS PROCESSES

Номер: US20200016580A1
Принадлежит:

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 138-. (canceled)39. A catalytic material comprising:(a) an OCM active catalyst; and {'br': None, 'sub': a', 'b', 'x', 'y, 'Ln1Ln2O(OH)'}, '(b) a second catalyst comprising the following formulawherein:Ln1 and Ln2 are each independently different lanthanide elements;O is oxygen;OH is hydroxy;a is a number greater than 0; andb, x and y are each independently numbers of 0 or greater, provided that at least one of x or y is greater than 0, andwherein the catalytic material comprises a methane conversion of greater than 20% and a C2 selectivity of greater than 50% when the catalytic material is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperatures ranging from about 550° C. to about 750° C.40. The catalytic material of claim 39 , wherein b and x are each independently numbers greater than 0 claim 39 , and y is 0.41. The catalytic material of claim 39 , wherein the OCM active catalyst is a bulk catalyst and the second catalyst is a nanostructured catalyst.42. The catalytic material of claim 39 , wherein the OCM active catalyst is a nanostructured catalyst.43. The catalytic material of claim 42 , wherein the OCM active catalyst is a nanowire catalyst.44. The catalytic material of claim 39 , wherein the second catalyst comprises a nanostructured catalyst comprising a lanthanum/neodymium oxide claim 39 , a lanthanum/cerium oxide claim 39 , a neodymium/cerium oxide claim 39 , a lanthanum/samarium oxide claim 39 , a neodymium/samarium oxide claim 39 , a europium/neodymium oxide claim 39 , a lanthanum/erbium oxide claim 39 , a neodymium/erbium oxide claim 39 , or a europium/lanthanum oxide.45. The catalytic material of claim 39 , wherein the ...

Подробнее
24-01-2019 дата публикации

HETEROGENEOUS CATALYSTS

Номер: US20190022626A1
Принадлежит:

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst comprising a mixed oxide base material , the mixed oxide comprising erbium (Er) and at least one further lanthanide element.2. The catalyst of claim 1 , wherein the mixed oxide comprises a physical blend of Er claim 1 , or an oxidized form thereof claim 1 , and the further lanthanide element claim 1 , or an oxidized form thereof.3. The catalyst of claim 1 , wherein the mixed oxide has the following formula (I):{'br': None, 'sub': x', 'y', 'z, 'LnErO\u2003\u2003 (I)'} Ln is the lanthanide element;', 'Er is erbium;', 'O is oxygen; and', 'x, y and z are each independently numbers greater than 0., 'wherein4. The catalyst of claim 3 , wherein x claim 3 , y and z are selected such that the overall charge of the catalyst is about 0.5. The catalyst of claim 3 , wherein x claim 3 , y and z are selected such that z is from 150% to 200% of the sum of x and y.6. The catalyst of claim 3 , wherein the mixed oxide is LnErOor LnErO.727-. (canceled)28. A bulk catalyst comprising a base material comprising an oxide of one or more lanthanide elements and a dopant combination selected from Sr/Ce claim 3 , Sr/Tb claim 3 , Sr/B and Sr/Hf/K.29. The catalyst of claim 28 , wherein the oxide has the following formula (III):{'br': None, 'sub': a', 'b', 'd', 'e', 'f', 'c, 'Ln1Ln2Ln3Ln4Ln5O\u2003\u2003 (III)'} Ln1, Ln2, Ln3, Ln4 and Ln5 are independently different lanthanide elements;', 'O is oxygen; and', 'a and c are each independently numbers greater than 0; and', 'b, d, e, and f are independently 0 or a number greater than 0., 'wherein30. The catalyst of claim 28 , wherein the dopant combination consists essentially of Sr/Ce claim 28 , Sr/Tb claim 28 , Sr/B or Sr/Hf/K.31. The catalyst of claim 28 , wherein the dopant ...

Подробнее
12-03-2015 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20150073192A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)86. A method for the preparation of ethane , ethylene or combinations thereof , the method comprising contacting a catalyst with a gas comprising methane , the catalyst comprising:{'sub': 4-x', 'x', '6, 'the formula Ln1Ln2O, wherein Ln1 and Ln2 are each independently a different lanthanide element, and x is a number ranging from greater than 0 to less than 4; and'}at least one doping element from groups 1-16, lanthanides, actinides or combinations thereof,{'sub': '2', 'wherein the catalyst further comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.'}87. The method of claim 86 , wherein the at least one doping element is selected from groups 1-4 claim 86 , 8 claim 86 , 13 claim 86 , 14 claim 86 , lanthanides claim 86 , actinides and combinations thereof.88. The method of claim 86 , wherein the at least one doping element is selected from groups 1-6 claim 86 , 8 claim 86 , 11 claim 86 , 13-15 claim 86 , lanthanides claim 86 , actinides and combinations thereof.89. The method of claim 86 , wherein the at least one doping element is a rare earth element.90. The method of claim 86 , wherein the at least one doping element is Na claim 86 , Mg claim 86 , Ca claim 86 , Sr claim 86 , Ga claim 86 , Sc claim 86 , Y claim 86 , Zr claim 86 , In claim 86 , Nd claim 86 , Eu claim 86 , Sm claim 86 , Ce claim 86 , Gd claim 86 , Hf claim 86 , Ho claim 86 , Tm claim 86 , W claim 86 , La claim 86 , K claim 86 , Dy claim 86 , In claim 86 , Cs claim 86 , S claim 86 , Zn claim 86 , Rb claim 86 ...

Подробнее
17-03-2016 дата публикации

CATALYSTS FOR NATURAL GAS PROCESSES

Номер: US20160074844A1
Принадлежит:

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 3. The catalytic material of claim 2 , wherein B is Ba claim 2 , Sr or Ca.4. The catalytic material of claim 2 , wherein A is Ce claim 2 , Ti claim 2 , Zr or Hf.5. The catalytic material of claim 2 , wherein α is greater than 0.6. The catalytic material of claim 5 , wherein the perovskite has the following formula:{'br': None, 'sup': '1', 'sub': α', 'm', 'n', 'p, 'EABO.'}7. The catalytic material of claim 2 , wherein Eis an element from group 2 or group 3 of the periodic table.8. The catalytic material of claim 2 , wherein the perovskite has the formula ABO.9. The catalytic material of claim 1 , wherein the catalyst has the formula Ln1Ln2O(OH).10. The catalytic material of claim 1 , wherein x is greater than zero.11. The catalytic material of claim 9 , wherein b and y are both 0.12. The catalytic material of claim 1 , wherein the catalyst is a nanostructured catalyst.13. The catalytic material of claim 12 , wherein the catalyst is a nanowire catalyst.14. The catalytic material of claim 1 , wherein the catalyst further comprises a dopant selected from one or more elements from groups 2 claim 1 , 6 and the lanthanides.15. The catalytic material of claim 14 , wherein the catalyst further comprises a dopant from each of groups 2 claim 14 , 6 and the lanthanides.16. The catalytic material of claim 14 , wherein the catalyst further comprises a dopant from each of groups 2 and 6.17. A method for performing a catalytic reaction claim 14 , the method comprising contacting a composition comprising a molten salt and a catalyst with a reactant gas claim 14 , thereby converting the reactant gas to a product gas claim 14 , wherein the reaction is oxidative coupling of methane or ...

Подробнее
14-03-2019 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20190077728A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 140-. (canceled)41. A catalyst comprising a mixed oxide of a lanthanide and tungsten , wherein the catalyst further comprises a sodium dopant and at least one doping element from groups 2 , 4-15 , lanthanides or combinations thereof , wherein the catalyst comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.42. The catalyst of claim 41 , wherein the lanthanide is Ce claim 41 , Pr claim 41 , Nd claim 41 , La claim 41 , Eu claim 41 , Sm or Yb.43. The catalyst of claim 41 , wherein the at least one doping element is Fe claim 41 , Co claim 41 , Mn claim 41 , Cu claim 41 , Ni claim 41 , Sr claim 41 , Ga claim 41 , Zr claim 41 , Pb claim 41 , Zn claim 41 , Cr claim 41 , Pt claim 41 , Al claim 41 , Nb claim 41 , La claim 41 , Ba claim 41 , Bi claim 41 , Sn claim 41 , In claim 41 , Ru claim 41 , P or combinations thereof.44. A catalyst comprising a rare earth oxide and two or more dopants claim 41 , wherein the catalyst comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less claim 41 , and wherein the dopant comprises Eu/Na claim 41 , Sr/Na claim 41 , Na/Zr/Eu/Ca claim 41 , Mg/Na claim 41 , Sr/Sm/Ho/Tm claim 41 , Sr/W claim 41 , Mg/La/K claim 41 , Na/K/Mg/Tm claim 41 , Na/Dy/K claim 41 , Na/La/Dy claim 41 , Na/La/Eu claim 41 , Na/La/Eu/In claim 41 , Na/La/K claim 41 , Na/La/Li/Cs claim 41 , K/La claim 41 , K/La/S claim 41 , K/Na claim ...

Подробнее
26-03-2015 дата публикации

NANOWIRE CATALYSTS AND METHODS FOR THEIR USE AND PREPARATION

Номер: US20150087875A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 1. A method for the preparation of ethane , ethylene or combinations thereof , the method comprising contacting a catalytic material with a gas comprising methane , wherein the catalytic material is in the form of a pressed pellet , extrudate or monolith and comprises:a) a plurality of catalytic nanowires, the catalytic nanowires comprising one or more doping elements; andb) a diluent or support selected from one or more alkaline earth metal compounds,and wherein the catalytic material has a C2+ yield above 5% when employed as catalytic material in the oxidative coupling of methane at an inlet temperature of 550° C. and an inlet pressure of about 2 atm in a fixed bed reactor with a gas-hour space velocity (GHSV) of at least about 20,000/hr.2. The method of claim 1 , wherein the catalytic materials is in the form of a pressure treated claim 1 , pressed pellet and comprises substantially no binder material.3. The method of claim 1 , wherein the catalytic material is in the form of a pressed pellet or extrudate and comprises pores greater than 20 nm in diameter.4. The method of claim 1 , wherein the alkaline earth metal compound is an alkaline earth metal oxide claim 1 , alkaline earth metal carbonate claim 1 , alkaline earth metal sulfate or alkaline earth metal phosphate.5. The method of claim 1 , wherein the alkaline earth metal compound is an alkaline earth metal carbonate claim 1 , alkaline earth metal sulfate or alkaline earth metal phosphate.6. The method of claim 1 , wherein the alkaline earth metal compound is MgO claim 1 , MgCO claim 1 , MgSO claim 1 , Mg(PO) claim 1 , MgAlO claim 1 , CaO claim 1 , CaCO claim 1 , CaSO claim 1 , Ca(PO) claim 1 , CaAlO claim 1 , SrO claim 1 , SrCO claim 1 , SrSO ...

Подробнее
05-04-2018 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20180093931A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)87. The catalyst of claim 86 , wherein A is from groups 2 claim 86 , 3 or 4.88. The catalyst of claim 86 , wherein A is Ce claim 86 , Pr claim 86 , Sr claim 86 , Ca claim 86 , Mg claim 86 , Y claim 86 , Zr or Ba.89. The catalyst of claim 86 , wherein B is from group 4.90. The catalyst of claim 86 , wherein B is Zr or Hf.91. The catalyst of claim 86 , wherein the dopant is Sr claim 86 , Mg or Ca.92. The catalyst of claim 86 , wherein the catalyst comprises one of the following formulas: Y/SrZrO claim 86 , SrHfO claim 86 , SrZrO claim 86 , Mg/SrHfO claim 86 , CaHfOor SrTbO.93. The catalyst of claim 86 , wherein the catalyst is a bulk catalyst.94. The catalyst of claim 86 , wherein the catalyst is a nanostructured catalyst.95. The catalyst of claim 94 , wherein the catalyst is a nanowire.96. A method for the oxidative coupling of methane claim 86 , the method comprising contacting methane with the catalyst of at temperatures ranging from about 550° C. to about 750° C. claim 86 , thereby converting the methane to C2 hydrocarbons at a methane conversion of greater than 20% and a C2 selectivity of greater than 50%.97. The method of claim 96 , wherein the method produces a product gas comprising less than 0.5% carbon monoxide. This invention is generally related to novel catalysts and, more specifically, to doped metal oxide catalysts useful as heterogeneous catalysts in a variety of catalytic reactions, such as the oxidative coupling of methane to C2 hydrocarbons.Catalysis is the process in which the rate of a chemical reaction is either increased or decreased by means of a catalyst. Positive catalysts increase the speed of a chemical reaction, ...

Подробнее
21-04-2016 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20160107143A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogeneous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)87. The catalyst of claim 86 , wherein A is Ba claim 86 , Zr claim 86 , Sr claim 86 , Sm claim 86 , Hf claim 86 , Gd claim 86 , Er claim 86 , Y claim 86 , Ca claim 86 , La claim 86 , Mg claim 86 , W claim 86 , B claim 86 , Tb or Ce.88. The catalyst of claim 86 , wherein B is Zn claim 86 , Hf claim 86 , Zr claim 86 , Al claim 86 , Ti claim 86 , Pr claim 86 , Nd claim 86 , Ce claim 86 , Sm claim 86 , Eu claim 86 , Gd claim 86 , Tb or Ho.89. The catalyst of claim 86 , wherein A is from group 2 claim 86 , and B is from group 4.90. The catalyst of claim 86 , wherein A is Ba claim 86 , Sr or Ca.91. The catalyst of claim 86 , wherein B is Ti claim 86 , Zr or Hf.92. The catalyst of claim 86 , having the formula ABO.93. The catalyst of claim 86 , comprising one or more dopant from group 2.94. The catalyst of claim 86 , comprising one or more dopant from group 3.95. The catalyst of claim 86 , comprising one or more dopant from the lanthanides.96. The catalyst of claim 86 , wherein the dopant is Sr claim 86 , Y claim 86 , La claim 86 , Nd claim 86 , Ca claim 86 , Mg or Ce or a combinations thereof.97. The catalyst of claim 86 , comprising the formula BaZrO claim 86 , SrZrO claim 86 , SrAlO claim 86 , SrCeO claim 86 , SrHfO claim 86 , CaHfO claim 86 , SrTbOor BaTiO.98. The catalyst of claim 86 , wherein the catalyst is a bulk catalyst.99. The catalyst of claim 86 , wherein the catalyst is a nanostructured catalyst.100. The catalyst of claim 99 , wherein the catalyst is a nanowire.101. A catalytic material comprising the catalyst of in combination with a support or carrier.102. The catalytic material of claim 101 , in the form of a formed aggregate. ...

Подробнее
09-04-2020 дата публикации

POLYMER TEMPLATED NANOWIRE CATALYSTS

Номер: US20200109094A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are prepared by polymer templated methods and are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to ethane and/or ethylene. Related methods for use and manufacture of the same are also disclosed. 133.-. (canceled)34. A process for the preparation of ethylene from methane comprising contacting a mixture comprising oxygen and methane with a catalytic material comprising nanowires comprising a plurality of metal oxides (MO) , metal oxy-hydroxides (MOOH) , metal oxycarbonates (MO(CO)) or metal carbonates (M(CO)) or combinations thereof , the nanowires prepared by a method comprising:a) providing a solution comprising a polymer template; and{'sub': m', 'n', 'p, '(b) introducing at least one metal ion and at least one anion to the solution under conditions and for a time sufficient to allow for nucleation and growth of nanowires comprising a plurality of metal salts (MXZ) on the polymer template,'}wherein:M is, at each occurrence, independently a metal element from any of Groups 1 through 7, lanthanides or actinides;X is, at each occurrence, independently hydroxide, carbonate, bicarbonate, phosphate, hydrogenphosphate, dihydrogenphosphate, sulfate, nitrate or oxalate;Z is O;n, m, x and y are each independently a number from 1 to 100; andp is a number from 0 to 100.35. The process of claim 34 , wherein the polymer template is functionalized with at least one of amine claim 34 , carboxylic acid claim 34 , sulfate claim 34 , alcohol or thiol groups.36. The process of claim 35 , wherein the polymer template comprises a hydrocarbon polymer.37. The process of claim 36 , wherein the polymer template comprises polystyrene.38. The process of claim 34 , wherein the method further comprises converting the nanowires comprising the plurality of metal salts (MXZ) to the nanowires comprising the plurality of metal oxides (MO) claim 34 , metal oxy-hydroxides (MOOH) ...

Подробнее
05-05-2016 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20160122261A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185-. (canceled)86. A catalyst comprising the following formula:{'br': None, 'sub': '3', 'ABO;'} A is an element from the lanthanides or group 2, 3 or 4 of the periodic table;', 'B is an element from groups 4, 12 or 13 of the periodic table or Ce, Eu, Gd, Tb or Ho; and', 'O is oxygen,, 'whereinthe catalyst further comprising one or more dopant from any one of groups 2 or 3, and wherein the catalyst further comprises a methane conversion of greater than 20% and a C2 selectivity of greater than 50% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperatures ranging from about 550° C. to about 750° C., and provided that A and B are not the same.87. The catalyst of claim 86 , wherein A is from groups 2 claim 86 , 3 or 4.88. The catalyst of claim 86 , wherein A is Ce claim 86 , Pr claim 86 , Sr claim 86 , Ca claim 86 , Mg claim 86 , Y claim 86 , Zr or Ba.89. The catalyst of claim 86 , wherein B is from group 4.90. The catalyst of claim 86 , wherein B is Zr or Hf.91. The catalyst of claim 86 , wherein the dopant is Sr. Mg or Ca.92. The catalyst of claim 86 , wherein the catalyst comprises one of the following formulas: Y/SrZrO claim 86 , SrHfO claim 86 , SrZrO claim 86 , Mg/SrHfO claim 86 , CaHfOor SrTbO.93. The catalyst of claim 86 , wherein the catalyst is a bulk catalyst.94. The catalyst of claim 86 , wherein the catalyst is a nanostructured catalyst.95. The catalyst of claim 94 , wherein the catalyst is a nanowire.96. A catalytic material comprising the catalyst of in combination with a support or carrier.97. The catalytic material of claim 96 , in the form of a formed aggregate.98. The catalytic ...

Подробнее
03-05-2018 дата публикации

CATALYSTS FOR NATURAL GAS PROCESSES

Номер: US20180117570A1
Принадлежит:

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed. 1189-. (canceled)192. The catalytic material of claim 191 , wherein B is Ba claim 191 , Sr or Ca.193. The catalytic material of claim 191 , wherein A is Ce claim 191 , Ti claim 191 , Zr or Hf.194. The catalytic material of claim 191 , wherein a is greater than 0.195. The catalytic material of claim 194 , wherein the perovskite has the following formula:{'br': None, 'sup': '1', 'sub': α', 'm', 'n', 'p, 'EABO.'}196. The catalytic material of claim 191 , wherein Eis an element from group 2 or group 3 of the periodic table.197. The catalytic material of claim 191 , wherein the perovskite has the formula ABO.198. The catalytic material of claim 190 , wherein x is greater than zero.199. The catalytic material of claim 190 , wherein b and y are both 0.200. The catalytic material of claim 190 , wherein the catalyst is a nanostructured catalyst.201. The catalytic material of claim 200 , wherein the catalyst is a nanowire catalyst.202. The catalytic material of claim 190 , wherein the catalyst further comprises a dopant selected from one or more elements from groups 2 claim 190 , 6 and the lanthanides.203. The catalytic material of claim 202 , wherein the catalyst further comprises a dopant from each of groups 2 claim 202 , 6 and the lanthanides.204. The catalytic material of claim 202 , wherein the catalyst further comprises a dopant from each of groups 2 and 6. This invention is generally related to catalysts and catalytic forms and formulations for use in natural gas processes, such as the oxidative coupling of methane.Catalysis is the process in which the rate of a chemical reaction is either increased or decreased by means of a catalyst. Positive catalysts lower the rate- ...

Подробнее
03-05-2018 дата публикации

NANOWIRE CATALYSTS AND METHODS FOR THEIR USE AND PREPARATION

Номер: US20180118637A1
Принадлежит:

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 141-. (canceled)42. A method for the preparation of ethane , ethylene or combinations thereof , the method comprising contacting a catalytic material with a gas comprising methane , wherein the catalytic material comprises a plurality of catalytic nanowires and a diluent or support , the diluent or support comprising an alkaline earth metal compound.43. The method of claim 42 , wherein the catalytic material is in the form of a pressed pellet claim 42 , extrudate or monolith.44. The method of claim 42 , wherein the catalytic material is in the form of a pressed pellet.45. The method of claim 42 , wherein the catalytic material is in the form of an extrudate.46. The method of claim 42 , wherein the catalytic material is in the form of a monolith.47. The method of claim 42 , wherein the catalytic nanowires comprise one or more doping elements.48. The method of claim 42 , wherein the catalytic material is in the form of a pressure treated claim 42 , pressed pellet and comprises substantially no binder material.49. The method of claim 42 , wherein the catalytic material is in the form of a pressed pellet or extrudate and comprises pores greater than 20 nm in diameter.50. The method of claim 42 , wherein the alkaline earth metal compound is an alkaline earth metal oxide claim 42 , alkaline earth metal carbonate claim 42 , alkaline earth metal sulfate or alkaline earth metal phosphate.51. The method of claim 42 , wherein the alkaline earth metal compound is an alkaline earth metal carbonate claim 42 , alkaline earth metal sulfate or alkaline earth metal phosphate.52. The method of claim 42 , wherein the diluent or support comprises MgO claim 42 , MgCO claim 42 , MgSO claim 42 , Mg(PO) claim 42 , MgAlO claim ...

Подробнее
18-09-2014 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20140274671A1
Принадлежит: SILURIA TECHNOLOGIES, INC.

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst comprising a mixed oxide of magnesium and manganese , wherein the catalyst further comprises lithium and boron dopants and at least one doping element from groups 4 , 9 , 12 , 13 or combinations thereof , wherein the catalyst comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.2. The catalyst of claim 1 , wherein the catalyst further comprises a sodium dopant.3. The catalyst of claim 1 , wherein the at least one doping element is cobalt.4. The catalyst of claim 1 , wherein the at least one doping element is gallium.5. The catalyst of any of claim 1 , wherein the catalyst further comprises at least one additional doping element from group 2.6. The catalyst of claim 5 , wherein the at least one additional doping element is beryllium claim 5 , barium claim 5 , hafnium or aluminum.7. A catalyst comprising a mixed oxide of manganese and tungsten claim 5 , wherein the catalyst further comprises a sodium dopant and at least one doping element from groups 2 claim 5 , 16 or combinations thereof.8. The catalyst of claim 7 , wherein the catalyst comprises a Cselectivity of greater than 50% and a methane conversion of greater than 20% when the catalyst is employed as a heterogenous catalyst in the oxidative coupling of methane at a temperature of 750° C. or less.9. The catalyst of claim 7 , wherein the doping element is barium claim 7 , beryllium or tellurium.10. A catalyst comprising an oxide of a rare earth element claim 7 , wherein the catalyst further comprises at least one doping ...

Подробнее
13-08-2015 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20150224482A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 185.-. (canceled)86. A catalyst comprising an oxide of a rare earth element , the catalyst comprising:{'sub': 4-x', 'x', '6, 'the formula Ln1Ln2O, wherein Ln1 and Ln2 are each independently a different lanthanide element, and x is a number ranging from greater than 0 to less than 4; and'}at least one doping element from one of groups 1-16, lanthanides, actinides or combinations thereof,{'sub': '2', 'wherein the catalyst further comprises a Cselectivity of greater than 50% and a methane conversion of greater than 10% when the catalyst is employed as a heterogeneous catalyst in the oxidative coupling of methane at a temperature of 700° C. or less.'}87. The catalyst of claim 86 , wherein the at least one doping element is selected from groups 1-4 claim 86 , 8 claim 86 , 13 claim 86 , 14 claim 86 , lanthanides claim 86 , actinides and combinations thereof.88. The catalyst of claim 86 , wherein the at least one doping element is selected from groups 1-6 claim 86 , 8 claim 86 , 11 claim 86 , 13-15 claim 86 , lanthanides claim 86 , actinides and combinations thereof.89. The catalyst of claim 86 , wherein the at least one doping element is a rare earth element.90. The catalyst of claim 86 , wherein the at least one doping element is Na claim 86 , Mg claim 86 , Ca claim 86 , Sr claim 86 , Ga claim 86 , Sc claim 86 , Y claim 86 , Zr claim 86 , In claim 86 , Nd claim 86 , Eu claim 86 , Sm claim 86 , Ce claim 86 , Gd claim 86 , Hf claim 86 , Ho claim 86 , Tm claim 86 , W claim 86 , La claim 86 , K claim 86 , Dy claim 86 , In claim 86 , Cs claim 86 , S claim 86 , Zn claim 86 , Rb claim 86 , Ba claim 86 , Yb claim 86 , Ni claim 86 , Lu claim 86 , Ta claim 86 , P claim ...

Подробнее
05-11-2015 дата публикации

HETEROGENEOUS CATALYSTS

Номер: US20150314267A1
Принадлежит:

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C hydrocarbons. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst comprising a mixed oxide base material , the mixed oxide comprising erbium (Er) and at least one further lanthanide element.2. The catalyst of claim 1 , wherein the mixed oxide comprises a physical blend of Er claim 1 , or an oxidized form thereof claim 1 , and the further lanthanide element claim 1 , or an oxidized form thereof.45-. (canceled)6. The catalyst of claim 1 , wherein the mixed oxide is LnErOor LnErO.7. A catalyst comprising a mixed oxide base material claim 1 , the mixed oxide base material comprising two different lanthanide elements claim 1 , provided that one of the lanthanide elements is not lanthanum when the other lanthanide element is neodymium.910-. (canceled)11. A catalyst comprising a mixed oxide base material claim 1 , the mixed oxide base material comprising three different lanthanide elements.13. The catalyst of claim 1 , wherein the mixed oxide base material comprises an oxide claim 1 , hydroxide claim 1 , oxy-hydroxide claim 1 , carbonate claim 1 , oxy-carbonate claim 1 , hydroxy carbonate or oxy-hydroxy-carbonate claim 1 , or combinations thereof.14. The catalyst of claim 1 , further comprising at least one doping element.1517-. (canceled)18. The catalyst of claim 14 , further comprising a second doping element.1920-. (canceled)21. The catalyst of claim 1 , wherein the catalyst is a nanowire catalyst.22. A catalyst comprising a base material comprising an oxide of one or more lanthanide elements and a dopant combination selected from Sr/Sm claim 1 , Sr/Gd claim 1 , Sr/Dy claim 1 , Sr/Er claim 1 , Sr/Lu claim 1 , Sr/Ba/B claim 1 , Ba/B claim 1 , Ba/Sr claim 1 , Er/W claim 1 , Sr/K claim 1 , Ba/Ce claim 1 , Ba/Hf claim 1 , Ga/Mg claim 1 , Mg/Er claim 1 , Y/Ba claim 1 , ...

Подробнее
26-11-2020 дата публикации

Heterogeneous catalysts

Номер: US20200368725A1
Принадлежит: Lummus Technology Inc

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C 2+ hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
03-12-2020 дата публикации

CATALYSTS FOR PETROCHEMICAL CATALYSIS

Номер: US20200377429A1
Принадлежит:

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed. 1. A catalyst blend comprising at least one first catalyst and at least one second catalyst , wherein the at least one first catalyst has a first oxidative coupling of methane (OCM) activity at a first temperature , and the at least one second catalyst has a second OCM activity which is lower than the first OCM activity at the first temperature , and wherein the second OCM activity is increased at a second temperature which is higher than the first temperature.2. The catalyst blend of claim 1 , wherein the first catalyst has a C2 yield of greater than 5% at temperatures less than 700° C. in the OCM reaction.3. The catalyst blend of claim 1 , wherein the second catalyst has a C2 yield of less than 5% at temperatures less than 700° C. in the OCM reaction.4. The catalyst blend of claim 1 , wherein the first catalyst has a C2 yield of greater than 5% at temperatures less than 600° C. in the OCM reaction.5. The catalyst blend of claim 1 , wherein the second catalyst has a C2 yield of less than 5% at temperatures less than 600° C. in the OCM reaction.6. The catalyst blend of claim 1 , wherein the first catalyst has a C2 yield of greater than 10% at temperatures less than 700° C. in the OCM reaction.7. The catalyst blend of claim 1 , wherein the second catalyst has a C2 yield of less than 1% at temperatures less than 700° C. in the OCM reaction.8. The catalyst blend of claim 1 , further comprising a support material.9. The catalyst blend of claim 8 , wherein the support material comprises AlPO claim 8 , AlO claim 8 , SiO—AlO claim 8 , CaO claim 8 , TiO claim 8 , ZrO claim 8 , MgO claim 8 , SiO claim 8 , ZrO claim 8 , HfO claim 8 , InO claim 8 , SiC or ...

Подробнее
21-09-2021 дата публикации

Nanowire catalysts and methods for their use and preparation

Номер: CA2856310C
Принадлежит: LUMMUS TECHNOLOGY LLC

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the nanowires are also disclosed.

Подробнее
18-09-2014 дата публикации

Catalysts for petrochemical catalysis

Номер: WO2014143880A1
Принадлежит: SILURIA TECHNOLOGIES, INC.

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogeneous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
05-11-2015 дата публикации

Heterogeneous catalysts

Номер: CA2947483A1
Принадлежит: Siluria Technologies Inc

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2+ hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
26-05-2021 дата публикации

Catalysts for natural gas processes

Номер: EP3825001A1
Принадлежит: Lummus Technology Inc

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
30-01-2014 дата публикации

Nanowire catalysts and methods for their use and preparation

Номер: WO2013082318A3
Принадлежит: SILURIA TECHNOLOGIES, INC.

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the nanowires are also disclosed.

Подробнее
30-12-2014 дата публикации

Catalysts for petrochemical catalysis

Номер: US8921256B2
Принадлежит: Siluria Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
01-05-2018 дата публикации

Heterogeneous catalysts

Номер: US9956544B2
Принадлежит: Siluria Technologies Inc

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C 2+ hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
19-05-2020 дата публикации

Catalysts for petrochemical catalysis

Номер: US10654769B2
Принадлежит: Siluria Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
08-05-2018 дата публикации

Catalysts for petrochemical catalysis

Номер: US9963402B2
Принадлежит: Siluria Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
24-02-2015 дата публикации

Nanowire catalysts and methods for their use and preparation

Номер: US8962517B2
Принадлежит: Siluria Technologies Inc

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
03-08-2021 дата публикации

Nanowire catalysts and methods for their use and preparation

Номер: US11078132B2
Принадлежит: LUMMUS TECHNOLOGY LLC

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
15-12-2020 дата публикации

Catalysts for petrochemical catalysis

Номер: US10865166B2
Принадлежит: Siluria Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogeneous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
04-06-2019 дата публикации

Catalysts for petrochemical catalysis

Номер: US10308565B2
Принадлежит: Silura Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
22-09-2020 дата публикации

Heterogeneous catalysts

Номер: US10780420B2
Принадлежит: Lummus Technology Inc

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2+ hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
11-05-2021 дата публикации

Catalysts for natural gas processes

Номер: US11000835B2
Принадлежит: Lummus Technology Inc

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
28-05-2019 дата публикации

Catalysts for natural gas processes

Номер: US10300465B2
Принадлежит: Siluria Technologies Inc

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
21-12-2017 дата публикации

Catalysts for oxidative coupling of methane

Номер: AU2017203318B2
Принадлежит: Lummus Technology Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
04-05-2017 дата публикации

Nanowire catalysts and methods for their use and preparation

Номер: AU2012345913B2
Принадлежит: Lummus Technology Inc

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the nanowires are also disclosed.

Подробнее
18-09-2014 дата публикации

Catalysts for petrochemical catalysis

Номер: CA2902192A1
Принадлежит: Siluria Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogeneous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
09-06-2016 дата публикации

Catalysts for oxidative coupling of methane and oxidative dehydrogenation of ehtane

Номер: WO2016044428A3
Принадлежит: SILURIA TECHNOLOGIES, INC.

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
06-06-2013 дата публикации

Nanowire catalysts and methods for their use and preparation

Номер: CA2856310A1
Принадлежит: Siluria Technologies Inc

Nanowires useful as heterogeneous catalysts are provided. The nanowire catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons. Related methods for use and manufacture of the nanowires are also disclosed.

Подробнее
20-10-2022 дата публикации

Process for purification and conversion of carbon dioxide using renewable energy

Номер: WO2022220892A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

The present invention is generally directed to processes and systems for the purification and conversion of CO2 into low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol% CO 2 . In certain cases, the CO 2 stream is processed to make low carbon fuels and chemicals. In this process at least a portion of the CO 2 is reacted with a stream comprising H2 in a Reverse Water Gas Shift (RWGS) reactor to produce a product stream that comprises CO.

Подробнее
29-11-2012 дата публикации

Catalysts for petrochemical catalysis

Номер: CA2837201A1
Принадлежит: Siluria Technologies Inc

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
20-10-2022 дата публикации

Process for purification and conversion of carbon dioxide using renewable energy

Номер: US20220333015A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to processes and systems for the purification and conversion of CO 2 into low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol % CO 2 . In certain cases, the CO 2 stream is processed to make low carbon fuels and chemicals. In this process at least a portion of the CO 2 is reacted with a stream comprising H 2 in a Reverse Water Gas Shift (RWGS) reactor to produce a product stream that comprises CO.

Подробнее
13-04-2017 дата публикации

Catalysts for oxidative coupling of methane and oxidative dehydrogenation of ethane

Номер: AU2015317805A1
Принадлежит: Siluria Technologies Inc

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
18-02-2016 дата публикации

Lanthanide based mixed oxide heterogeneous catalysts

Номер: WO2015168601A3
Принадлежит: SILURIA TECHNOLOGIES, INC.

Heterogeneous catalysts with optional dopants are provided. The catalysts are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane to C 2+ hydrocarbons. Related methods for use and manufacture of the same are also disclosed.

Подробнее
18-05-2023 дата публикации

CO2 hydrogenation catalysts for the commercial production of syngas

Номер: US20230150823A1
Принадлежит: Individual

The present invention is generally directed to the production of low-carbon syngas from captured CO 2 and renewable H 2 . The H 2 is generated from water using an electrolyzer powered by renewable electricity, or from any other method of low-carbon H 2 production. The improved catalysts use low-cost metals, they can be produced economically in commercial quantities, and they are chemically and physically stable up to 2,100° F. CO 2 conversion is between 80% and 100% with CO selectivity of greater than 99%. The catalysts don't sinter or form coke when converting H 2 :CO 2 mixtures to syngas in the operating ranges of 1,300-1,800° F., pressures of 75-450 psi, and space velocities of 2,000-100,000 hr −1 . The catalysts are stable, exhibiting between 0 and 1% CO 2 conversion decline per 1,000 hrs. The syngas can be used for the synthesis of low-carbon fuels and chemicals, or for the production of purified H 2 . The H 2 can be used at the production site for the synthesis of low-carbon chemical products or compressed for transportation use.

Подробнее
24-03-2016 дата публикации

Catalysts for oxidative coupling of methane and oxidative dehydrogenation of ethane

Номер: CA2960555A1
Принадлежит: Siluria Technologies Inc

Catalysts, catalytic forms and formulations, and catalytic methods are provided. The catalysts and catalytic forms and formulations are useful in a variety of catalytic reactions, for example, the oxidative coupling of methane. Related methods for use and manufacture of the same are also disclosed.

Подробнее
29-02-2024 дата публикации

One-step process for the production of hydrocarbons from carbon dioxide

Номер: WO2024043941A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

The present invention are new and improved processes and catalysts that can efficiently facilitate the direct carbon dioxide conversion reaction with hydrogen to hydrocarbons in a single reactor at temperatures less than 450°C and more preferably at temperatures from 250°C to 325°C. Carbon dioxide is utilized from stationary sources or from direct air capture. Hydrogen is produced by the electrolysis of water using renewable or low carbon electricity.

Подробнее
26-10-2023 дата публикации

Process for purification and conversion of carbon dioxide using renewable energy

Номер: AU2022256276A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to processes and systems for the purification and conversion of CO2 into low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol% CO

Подробнее
14-03-2024 дата публикации

Systems and methods for producing negative carbon intensity hydrocarbon products

Номер: WO2024054241A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

Provided herein are systems and methods for controlling the production of negative carbon- intensity liquid hydrocarbons (e.g., for fuels and chemicals). In various aspects, the methods utilize a feedstock having a negative carbon intensity, produce a co-product from the feedstock, sequester a portion of the CO 2 derived from the feedstock, or utilize a portion of the O 2 in a process that consumes O 2 and emits CO 2 .

Подробнее
21-03-2024 дата публикации

Systems and methods for producing negative carbon intensity hydrocarbon products

Номер: US20240093105A1
Принадлежит: Infinium Technology LLC

Provided herein are systems and methods for controlling the production of negative carbon-intensity liquid hydrocarbons (e.g., for fuels and chemicals). In various aspects, the methods utilize a feedstock having a negative carbon intensity, produce a co-product from the feedstock, sequester a portion of the CO 2 derived from the feedstock, or utilize a portion of the O 2 in a process that consumes O 2 and emits CO 2 .

Подробнее
02-01-2024 дата публикации

Thermally integrated process for the production of liquid fuels with a solid oxide electrolyzer

Номер: US11859135B2
Принадлежит: Infinium Technology LLC

Production of fuels from low carbon electricity and from carbon dioxide by the use of a solid oxide electrolysis cell (SOEC) and Fischer-Tropsch is shown. Fischer-Tropsch is an exothermic reaction that can be used to produce steam. Steam produced from the Liquid Fuel Production (LFP) reactor system, where the Fischer-Tropsch reaction occurs, is used as feed to the SOEC. The higher temperature steam improves the efficiency of the overall electrolysis system. The integration of the LFP steam improves the efficiency of the electrolysis because the heat of vaporization for the liquid water does not have to be supplied by the electrolyzer.

Подробнее
11-01-2024 дата публикации

Process for the one-step conversion of carbon dioxide and renewable hydrogen to low-carbon methane

Номер: US20240010580A1
Принадлежит: Infinium Technology LLC

The objective of the present invention is to take advantage of new and improved processes and catalysts that can facilitate the efficient, direct CO2 conversion (CO2C) reaction to e-methane at temperatures less than about 350° C. in one step.

Подробнее
21-11-2023 дата публикации

Catalytic reactor for the conversion of carbon dioxide and hydrogen to syngas

Номер: US11819815B2
Принадлежит: Infinium Technology LLC

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800° F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800° F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst.

Подробнее
02-01-2024 дата публикации

Systems and methods for controlling a Power-to-X process to reduce feedstock costs

Номер: US11857938B2
Принадлежит: Infinium Technology LLC

Provided herein are systems and methods for controlling production of low-carbon liquid fuels and chemicals. In an aspect, provided herein is a method controlling a process that produces e-fuels. In another aspect, provided herein is a system for producing an e-fuel.

Подробнее
22-02-2024 дата публикации

One-step process for the production of hydrocarbons from carbon dioxide

Номер: US20240059978A1
Принадлежит: Infinium Technology LLC

The present invention are new and improved processes and catalysts that can efficiently facilitate the direct carbon dioxide conversion reaction with hydrogen to hydrocarbons in a single reactor at temperatures less than 450° C. and more preferably at temperatures from 250° C. to 325° C. Carbon dioxide is utilized from stationary sources or from direct air capture. Hydrogen is produced by the electrolysis of water using renewable or low carbon electricity.

Подробнее
21-02-2024 дата публикации

Process for purification and conversion of carbon dioxide using renewable energy

Номер: EP4323085A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to processes and systems for the purification and conversion of CO2 into low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol% CO 2 . In certain cases, the CO 2 stream is processed to make low carbon fuels and chemicals. In this process at least a portion of the CO 2 is reacted with a stream comprising H2 in a Reverse Water Gas Shift (RWGS) reactor to produce a product stream that comprises CO.

Подробнее
22-02-2024 дата публикации

Catalytic reactor for the conversion of carbon dioxide and hydrogen to syngas

Номер: US20240058778A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800° F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800° F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst. Electrical resistive heating elements are integrated into the catalytic bed of the reactor so that the internal temperature decreases by no more than 100° F. from the entrance at any point within the reactor. The catalytic process exhibits a reduction in performance of less than 0.5% per 1000 operational hours.

Подробнее
11-01-2024 дата публикации

Improved process for the one-step conversion of carbon dioxide and renewable hydrogen to low-carbon methane

Номер: WO2024010614A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

The objective of the present invention is to take advantage of new and improved processes and catalysts that can facilitate the efficient, direct CO2 conversion (CO2C) reaction to e-methane at temperatures less than about 350°C in one step.

Подробнее
20-10-2022 дата публикации

Process for purification and conversion of carbon dioxide using renewable energy

Номер: CA3215721A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to processes and systems for the purification and conversion of CO2 into low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol% CO2. In certain cases, the CO2 stream is processed to make low carbon fuels and chemicals. In this process at least a portion of the CO2 is reacted with a stream comprising H2 in a Reverse Water Gas Shift (RWGS) reactor to produce a product stream that comprises CO.

Подробнее
24-10-2023 дата публикации

Catalysts for petrochemical catalysis

Номер: US11795123B2
Принадлежит: LUMMUS TECHNOLOGY LLC

Metal oxide catalysts comprising various dopants are provided. The catalysts are useful as heterogenous catalysts in a variety of catalytic reactions, for example, the oxidative coupling of methane to C2 hydrocarbons such as ethane and ethylene. Related methods for use and manufacture of the same are also disclosed.

Подробнее
26-10-2023 дата публикации

Process for production of syngas and fuels from carbon dioxide using oxyfuel combustion

Номер: WO2023204877A2
Принадлежит: INFINIUM TECHNOLOGY, LLC

Syngas and liquid hydrocarbons are produced from synthesis gas. The synthesis gas is produced from a feed mixture of hydrogen and carbon dioxide. The feed mixture is heated to the reverse water gas shift (RWGS) reactor inlet temperature of 1400 to 1800°F or even more preferred to a RWGS reactor inlet temperature of 1550 to 1650°F. Some of the heat required to heat the feed mixture to the RWGS inlet temperature is supplied by the oxyfuel combustion of hydrogen or fuel with oxygen and minimizes the load onto electrical heaters or need for gas fired geaters. The high inlet temperature allows a high conversion of carbon dioxide to carbon monoxide. Various fuels can be used including hydrogen, hydrocarbons, oxygenates, or carbon monoxide can be used as combustion fuel. The carbon monoxide produced can further be reacted with hydrogen to produce hydrocarbon fuels and chemicals. The hydrocarbon fuels produced include sustainable aviation fuel (SAP) that meets ASTM D7566 specification and diesel fuel that meets ASTM D975 specification. The hydrogen and oxygen are produced from the electrolysis of water. The carbon dioxide can be captured from industrial point sources such as power plants, ethanol plants, steel mills, or other producers of carbon dioxide. Alternatively, the carbon dioxide can be captured from the atmosphere.

Подробнее
08-02-2024 дата публикации

Production and use of liquid fuel as a hydrogen and/or syngas carrier

Номер: AU2022324146A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to the efficient production of low-carbon methanol, ethanol or mixtures of methanol and ethanol from captured CO

Подробнее
26-10-2023 дата публикации

Process for production of syngas and fuels from carbon dioxide using oxyfuel combustion

Номер: US20230340347A1
Принадлежит: Infinium Technology LLC

Syngas and liquid hydrocarbons are produced from synthesis gas. The synthesis gas is produced from a feed mixture of hydrogen and carbon dioxide. The feed mixture is heated to the reverse water gas shift (RWGS) reactor inlet temperature of 1400 to 1800° F. or even more preferred to a RWGS reactor inlet temperature of 1550 to 1650° F. Some of the heat required to heat the feed mixture to the RWGS inlet temperature is supplied by the oxyfuel combustion of hydrogen or fuel with oxygen and minimizes the load onto electrical heaters or need for gas fired geaters. The high inlet temperature allows a high conversion of carbon dioxide to carbon monoxide. Various fuels can be used including hydrogen, hydrocarbons, oxygenates, or carbon monoxide can be used as combustion fuel. The carbon monoxide produced can further be reacted with hydrogen to produce hydrocarbon fuels and chemicals. The hydrocarbon fuels produced include sustainable aviation fuel (SAF) that meets ASTM D7566 specification and diesel fuel that meets ASTM D975 specification. The hydrogen and oxygen are produced from the electrolysis of water. The carbon dioxide can be captured from industrial point sources such as power plants, ethanol plants, steel mills, or other producers of carbon dioxide. Alternatively, the carbon dioxide can be captured from the atmosphere.

Подробнее
23-04-2024 дата публикации

Production of sustainable aviation fuel from CO2 and low-carbon hydrogen

Номер: US11965134B2
Принадлежит: Infinium Technology LLC

A process for the production of sustainable aviation fuel (SAF) with low carbon intensity. The jet fuel is produced from the reaction of hydrogen from the electrolysis of water with captured carbon dioxide. The hydrogen and carbon dioxide are reacted to product a stream comprising carbon monoxide. Hydrogen and carbon monoxide are reacted to produce n-alkanes. Alkanes are hydroisomerized to produce sustainable aviation fuel with low carbon intensity.

Подробнее
04-04-2024 дата публикации

Process for production of syngas and fuels from carbon dioxide using oxyfuel combustion

Номер: WO2023204877A3
Принадлежит: INFINIUM TECHNOLOGY, LLC

Syngas and liquid hydrocarbons are produced from synthesis gas. The synthesis gas is produced from a feed mixture of hydrogen and carbon dioxide. The feed mixture is heated to the reverse water gas shift (RWGS) reactor inlet temperature of 1400 to 1800°F. Some of the heat required to heat the feed mixture to the RWGS inlet temperature is supplied by the oxyfuel combustion of hydrogen or fuel with oxygen and minimizes the load onto electrical heaters or need for gas fired heaters. The high inlet temperature allows a high conversion of carbon dioxide to carbon monoxide. Various fuels can be used including hydrogen, hydrocarbons, oxygenates, or carbon monoxide can be used as combustion fuel. The carbon monoxide produced can further be reacted with hydrogen to produce hydrocarbon fuels and chemicals. The hydrogen and oxygen are produced from the electrolysis of water. The carbon dioxide can be captured from industrial point sources such as power plants, ethanol plants, steel mills, or other producers of carbon dioxide. Alternatively, the carbon dioxide can be captured from the atmosphere.

Подробнее
03-08-2023 дата публикации

Production of sustainable aviation fuel from co2 and low-carbon hydrogen

Номер: US20230242822A1
Принадлежит: Infinium Technology LLC

A process for the production of sustainable aviation fuel (SAF) with low carbon intensity. The jet fuel is produced from the reaction of hydrogen from the electrolysis of water with captured carbon dioxide. The hydrogen and carbon dioxide are reacted to product a stream comprising carbon monoxide. Hydrogen and carbon monoxide are reacted to produce n-alkanes. Alkanes are hydroisomerized to produce sustainable aviation fuel with low carbon intensity.

Подробнее
14-09-2023 дата публикации

Thermally integrated process for the production of liquid fuels with a solid oxide electrolyzer

Номер: US20230287274A1
Принадлежит: Infinium Technology LLC

Production of fuels from low carbon electricity and from carbon dioxide by the use of a solid oxide electrolysis cell (SOEC) and Fischer-Tropsch is shown. Fischer-Tropsch is an exothermic reaction that can be used to produce steam. Steam produced from the Liquid Fuel Production (LFP) reactor system, where the Fischer-Tropsch reaction occurs, is used as feed to the SOEC. The higher temperature steam improves the efficiency of the overall electrolysis system. The integration of the LFP steam improves the efficiency of the electrolysis because the heat of vaporization for the liquid water does not have to be supplied by the electrolyzer.

Подробнее
21-03-2024 дата публикации

Thermally integrated process for the production of liquid fuels with a solid oxide electrolyzer

Номер: US20240093097A1
Принадлежит: Infinium Technology LLC

Production of fuels from low carbon electricity and from carbon dioxide by the use of a solid oxide electrolysis cell (SOEC) and Fischer-Tropsch is shown. Fischer-Tropsch is an exothermic reaction that can be used to produce steam. Steam produced from the Liquid Fuel Production (LFP) reactor system, where the Fischer-Tropsch reaction occurs, is used as feed to the SOEC. The higher temperature steam improves the efficiency of the overall electrolysis system. The integration of the LFP steam improves the efficiency of the electrolysis because the heat of vaporization for the liquid water does not have to be supplied by the electrolyzer.

Подробнее
16-05-2024 дата публикации

Improved catalytic reactor for the conversion of carbon dioxide and hydrogen to syngas

Номер: AU2022390428A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800°F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800°F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst. Electrical resistive heating elements are integrated into the catalytic bed of the reactor so that the internal temperature decreases by no more than 100°F from the entrance at any point within the reactor. The catalytic process exhibits a reduction in performance of less than 0.5% per 1000 operational hours.

Подробнее
25-05-2023 дата публикации

Improved catalytic reactor for the conversion of carbon dioxide and hydrogen to syngas

Номер: CA3236706A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to a reactor for the production of low-carbon syngas from captured carbon dioxide and renewable hydrogen. The hydrogen is generated from water using an electrolyzer powered by renewable electricity or from any other method of low-carbon hydrogen production. The improved catalytic reactor is energy efficient and robust when operating at temperatures up to 1800°F. Carbon dioxide conversion efficiencies are greater than 75% with carbon monoxide selectivity of greater than 98%. The catalytic reactor is constructed of materials that are physically and chemically robust up to 1800°F. As a result, these materials are not reactive with the mixture of hydrogen and carbon dioxide or the carbon monoxide and steam products. The reactor materials do not have catalytic activity or modify the physical and chemical composition of the conversion catalyst. Electrical resistive heating elements are integrated into the catalytic bed of the reactor so that the internal temperature decreases by no more than 100°F from the entrance at any point within the reactor. The catalytic process exhibits a reduction in performance of less than 0.5% per 1000 operational hours.

Подробнее
14-03-2024 дата публикации

CO2 hydrogenation catalysts for the commercial production of syngas

Номер: US20240083755A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to the production of low-carbon syngas from captured CO2 and renewable H2. The H2 is generated from water using an electrolyzer powered by renewable electricity, or from any other method of low-carbon H2 production. The improved catalysts use low-cost metals, they can be produced economically in commercial quantities, and they are chemically and physically stable up to 2,100° F. CO2 conversion is between 80% and 100% with CO selectivity of greater than 99%. The catalysts don't sinter or form coke when converting H2:CO2 mixtures to syngas in the operating ranges of 1,300-1,800° F., pressures of 75-450 psi, and space velocities of 2,000-100,000 hr−1. The catalysts are stable, exhibiting between 0 and 1% CO2 conversion decline per 1,000 hrs. The syngas can be used for the synthesis of low-carbon fuels and chemicals, or for the production of purified H2. The H2 can be used at the production site for the synthesis of low-carbon chemical products or compressed for transportation use.

Подробнее
29-02-2024 дата публикации

Systems and methods for controlling a power-to-x process to reduce feedstock costs

Номер: US20240066492A1
Принадлежит: Infinitum Technology LLC

Provided herein are systems and methods for controlling production of low-carbon liquid fuels and chemicals. In an aspect, provided herein is a method controlling a process that produces e-fuels. In another aspect, provided herein is a system for producing an e-fuel.

Подробнее
16-05-2024 дата публикации

Systems and methods for controlling a power-to-x process to reduce feedstock costs

Номер: AU2022392161A1
Принадлежит: Infinium Technology LLC

Provided herein are systems and methods for controlling production of low-carbon liquid fuels and chemicals. In an aspect, provided herein is a method controlling a process that produces e-fuels. In another aspect, provided herein is a system for producing an e-fuel from constituent ingredients H2 and CO2, with H2 produced via electrolysis powered by renewable electrical energy.

Подробнее
25-05-2023 дата публикации

Systems and methods for controlling a power-to-x process to reduce feedstock costs

Номер: CA3236866A1
Принадлежит: Infinium Technology LLC

Provided herein are systems and methods for controlling production of low-carbon liquid fuels and chemicals. In an aspect, provided herein is a method controlling a process that produces e-fuels. In another aspect, provided herein is a system for producing an e-fuel from constituent ingredients H2 and CO2, with H2 produced via electrolysis powered by renewable electrical energy.

Подробнее
25-05-2023 дата публикации

Systems and methods for controlling a power-to-x process to reduce feedstock costs

Номер: WO2023091165A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

Provided herein are systems and methods for controlling production of low-carbon liquid fuels and chemicals. In an aspect, provided herein is a method controlling a process that produces e-fuels. In another aspect, provided herein is a system for producing an e-fuel from constituent ingredients H2 and CO2, with H2 produced via electrolysis powered by renewable electrical energy.

Подробнее
25-05-2023 дата публикации

Improved co2 hydrogenation catalysts for the commercial production of syngas

Номер: CA3236914A1
Принадлежит: Infinium Technology LLC

The present invention is directed to the production of low-carbon syngas from captured CO2 and renewable H2. The H2 is generated from water using an electrolyzer powered by renewable electricity, or from any other method of low-carbon H2 production. The improved catalysts use low-cost metals, they can be produced economically in commercial quantities, and they are chemically and physically stable up to 2,100 °F. CO2 conversion is between 80% and 100% with CO selectivity of greater than 99%. The catalysts don't sinter or form coke when converting H2.CO2 mixtures to syngas in the operating ranges of 1,300-1,800 °F, pressures of 75- 450 psi, and space velocities of 2,000-100,000 hr-1. The catalysts are stable, exhibiting between 0 and 1 % CO2 conversion decline per 1,000 hrs. The syngas can be used for the synthesis of low-carbon fuels and chemicals, or for the production of purified H2.

Подробнее
16-05-2024 дата публикации

Improved co2 hydrogenation catalysts for the commercial production of syngas

Номер: AU2022390055A1
Принадлежит: Infinium Technology LLC

The present invention is directed to the production of low-carbon syngas from captured CO2 and renewable H2. The H2 is generated from water using an electrolyzer powered by renewable electricity, or from any other method of low-carbon H2 production. The improved catalysts use low-cost metals, they can be produced economically in commercial quantities, and they are chemically and physically stable up to 2,100 °F. CO2 conversion is between 80% and 100% with CO selectivity of greater than 99%. The catalysts don't sinter or form coke when converting H2.CO2 mixtures to syngas in the operating ranges of 1,300-1,800 °F, pressures of 75- 450 psi, and space velocities of 2,000-100,000 hr-1. The catalysts are stable, exhibiting between 0 and 1 % CO2 conversion decline per 1,000 hrs. The syngas can be used for the synthesis of low-carbon fuels and chemicals, or for the production of purified H2.

Подробнее
12-06-2024 дата публикации

Production and use of liquid fuel as a hydrogen and/or syngas carrier

Номер: EP4380891A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to the efficient production of low-carbon methanol, ethanol or mixtures of methanol and ethanol from captured CO 2 and renewable H 2 at a generation site. The H 2 is generated from water using an electrolyzer powered by renewable electricity, or from any other means of low-carbon H 2 production. An improved catalyst and process is described that efficiently converts H 2 and CO 2 mixture to syngas in a one-step process, and alcohols, such as methanol and ethanol, are produced from the syngas in a second step. The liquid methanol and ethanol, which are excellent H 2 carriers, are transported to a production site, where another improved catalyst and process efficiently converts them to syngas. The syngas can then be used at the production site for the synthesis of low carbon fuels and chemicals, or to produce purified low carbon H 2 . The low carbon H 2 can be used at the production site for the synthesis of low-carbon chemical products or compressed for transportation use.

Подробнее
18-07-2024 дата публикации

Production and Use of Liquid Fuel as a Hydrogen and/or Syngas Carrier

Номер: US20240239654A1
Принадлежит: Infinium Technology LLC

The present invention is generally directed to the efficient production of low-carbon methanol, ethanol or mixtures of methanol and ethanol from captured CO2 and renewable H2 at a generation site. The H2 is generated from water using an electrolyzer powered by renewable electricity, or from any other means of low-carbon H2 production. An improved catalyst and process is described that efficiently converts H2 and CO2 mixture to syngas in a one-step process, and alcohols, such as methanol and ethanol, are produced from the syngas in a second step. The liquid methanol and ethanol, which are excellent H2 carriers, are transported to a production site, where another improved catalyst and process efficiently converts them to syngas. The syngas can then be used at the production site for the synthesis of low carbon fuels and chemicals, or to produce purified low carbon H2. The low carbon H2 can be used at the production site for the synthesis of low-carbon chemical products or compressed for transportation use.

Подробнее
25-05-2023 дата публикации

Improved co2 hydrogenation catalysts for the commercial production of syngas

Номер: WO2023091167A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

The present invention is directed to the production of low-carbon syngas from captured CO2 and renewable H2. The H2 is generated from water using an electrolyzer powered by renewable electricity, or from any other method of low-carbon H2 production. The improved catalysts use low-cost metals, they can be produced economically in commercial quantities, and they are chemically and physically stable up to 2,100 °F. CO2 conversion is between 80% and 100% with CO selectivity of greater than 99%. The catalysts don't sinter or form coke when converting H2.CO2 mixtures to syngas in the operating ranges of 1,300-1,800 °F, pressures of 75- 450 psi, and space velocities of 2,000-100,000 hr-1. The catalysts are stable, exhibiting between 0 and 1 % CO2 conversion decline per 1,000 hrs. The syngas can be used for the synthesis of low-carbon fuels and chemicals, or for the production of purified H2.

Подробнее
10-08-2023 дата публикации

Production of sustainable aviation fuel from co2 and low-carbon hydrogen

Номер: WO2023150001A1
Принадлежит: INFINIUM TECHNOLOGY, LLC

A process for the production of sustainable aviation fuel (SAP) with low carbon intensity. The jet fuel is produced from the reaction of hydrogen from the electrolysis of water with captured carbon dioxide. The hydrogen and carbon dioxide are reacted to product a stream comprising carbon monoxide. Hydrogen and carbon monoxide are reacted to produce n-alkanes. Alkanes are hydroisomerized to produce sustainable aviation fuel with low carbon intensity.

Подробнее
24-05-2024 дата публикации

Catalizadores de hidrogenacion de co 2 mejorados para la produccion comercial de gas sintetico.

Номер: MX2024005765A
Принадлежит: Infinium Tech Llc

La presente invención está dirigida generalmente a la producción de gas sintético bajo en carbono a partir de CO2 capturado y H2 renovable. El H2 se genera a partir de agua utilizando un electrolizador energizado por electricidad renovable, o a partir de cualquier otro método de producción de H2 bajo en carbono. Los catalizadores mejorados utilizan metales de bajo costo, pueden producirse económicamente en cantidades comerciales y son química y físicamente estables hasta los 1,148.89ºC (2,100ºF). La conversión de CO2 está entre el 80% y el 100% con una selectividad de CO superior al 99%. Los catalizadores no se sinterizan ni forman coque al convertir mezclas de H2:CO2 en gas sintético en los intervalos operativos de 704.44-982.22ºC (1,300-1,800ºF), presiones de 5.17-31.03 bar (75-450 psi) y velocidades espaciales de 2,000-100,000 h-1. Los catalizadores son estables, exhibiendo entre un 0 y un 1% de descenso de la conversión de CO2 por cada 1,000 horas. El gas sintético puede utilizarse para la síntesis de combustibles y productos químicos bajos en carbono, o para la producción de H2 purificado. El H2 puede utilizarse en el lugar de producción para la síntesis de productos químicos bajos en carbono o comprimirse para su uso en el transporte.

Подробнее
22-08-2024 дата публикации

Production of sustainable aviation fuel from co2 and low-carbon hydrogen

Номер: AU2023215182A1
Принадлежит: Infinium Technology LLC

A process for the production of sustainable aviation fuel (SAP) with low carbon intensity. The jet fuel is produced from the reaction of hydrogen from the electrolysis of water with captured carbon dioxide. The hydrogen and carbon dioxide are reacted to product a stream comprising carbon monoxide. Hydrogen and carbon monoxide are reacted to produce n-alkanes. Alkanes are hydroisomerized to produce sustainable aviation fuel with low carbon intensity.

Подробнее
24-09-2024 дата публикации

Process for purification and conversion of carbon dioxide using renewable energy

Номер: US12098329B2
Принадлежит: Infinium Technology LLC

The present invention is generally directed to processes and systems for the purification and conversion of CO2 into low-carbon or zero-carbon high quality fuels and chemicals using renewable energy. In one aspect, the present invention provides a process for producing a stream comprising at least 90 mol % CO2. In certain cases, the CO2 stream is processed to make low carbon fuels and chemicals. In this process at least a portion of the CO2 is reacted with a stream comprising H2 in a Reverse Water Gas Shift (RWGS) reactor to produce a product stream that comprises CO.

Подробнее
25-09-2024 дата публикации

<sup2/>? <sub2/>?2?improved cohydrogenation catalysts for the commercial production of syngas

Номер: EP4433206A1
Принадлежит: Infinium Technology LLC

The present invention is directed to the production of low-carbon syngas from captured CO2 and renewable H2. The H2 is generated from water using an electrolyzer powered by renewable electricity, or from any other method of low-carbon H2 production. The improved catalysts use low-cost metals, they can be produced economically in commercial quantities, and they are chemically and physically stable up to 2,100 °F. CO2 conversion is between 80% and 100% with CO selectivity of greater than 99%. The catalysts don't sinter or form coke when converting H2.CO2 mixtures to syngas in the operating ranges of 1,300-1,800 °F, pressures of 75- 450 psi, and space velocities of 2,000-100,000 hr-1. The catalysts are stable, exhibiting between 0 and 1 % CO2 conversion decline per 1,000 hrs. The syngas can be used for the synthesis of low-carbon fuels and chemicals, or for the production of purified H2.

Подробнее
17-10-2024 дата публикации

Production of Sustainable Aviation Fuel from CO2 and Low-Carbon Hydrogen

Номер: US20240343981A1
Принадлежит: Infinium Technology LLC

A process for the production of sustainable aviation fuel (SAF) with low carbon intensity. The jet fuel is produced from the reaction of hydrogen from the electrolysis of water with captured carbon dioxide. The hydrogen and carbon dioxide are reacted to product a stream comprising carbon monoxide. Hydrogen and carbon monoxide are reacted to produce n-alkanes. Alkanes are hydroisomerized to produce sustainable aviation fuel with low carbon intensity.

Подробнее
23-08-2024 дата публикации

Catalizadores de hidrogenación de co2 mejorados para la producción comercial de gas de síntesis

Номер: CL2024001393A1
Принадлежит: Infinium Tech Llc

La presente invención se dirige en general a la producción de gas de síntesis bajo en carbono a partir de CO2 capturado y H2 renovable. El H2 se genera a partir del agua mediante un electrolizador alimentado con electricidad renovable, o a partir de cualquier otro procedimiento de producción de H2 con bajas emisiones de carbono. Los catalizadores mejorados utilizan metales de bajo coste, pueden producirse económicamente en cantidades comerciales y son química y físicamente estables hasta los 1.149 C (2.100 F). La conversión de CO2 se sitúa entre el 80 por ciento y el 100 por ciento, con una selectividad de CO superior al 99 por ciento. Los catalizadores no se sinterizan ni forman coque al convertir mezclas de H2:CO2 en gas de síntesis en intervalos operativos de 704-982 C (1.300-1.800 F), presiones de 5,17- 31,03 Bar (75-450 psi) y velocidades espaciales de 2.000-100.000 h-1. Los catalizadores son estables y presentan un descenso de la conversión de CO2 de entre el 0 y el 1 por ciento cada 1.000 horas. El gas de síntesis puede utilizarse para la síntesis de combustibles y productos químicos bajos en carbono, o para la producción deH2purificado. El H2 puede utilizarse en el lugar de producción para la síntesis de productos químicos bajos en carbono o comprimirse para su uso en el transporte.

Подробнее
31-10-2024 дата публикации

Process for production of syngas and fuels from carbon dioxide using oxyfuel combustion

Номер: AU2023257193A1
Принадлежит: Infinium Technology LLC

Syngas and liquid hydrocarbons are produced from synthesis gas. The synthesis gas is produced from a feed mixture of hydrogen and carbon dioxide. The feed mixture is heated to the reverse water gas shift (RWGS) reactor inlet temperature of 1400 to 1800°F or even more preferred to a RWGS reactor inlet temperature of 1550 to 1650°F. Some of the heat required to heat the feed mixture to the RWGS inlet temperature is supplied by the oxyfuel combustion of hydrogen or fuel with oxygen and minimizes the load onto electrical heaters or need for gas fired geaters. The high inlet temperature allows a high conversion of carbon dioxide to carbon monoxide. Various fuels can be used including hydrogen, hydrocarbons, oxygenates, or carbon monoxide can be used as combustion fuel. The carbon monoxide produced can further be reacted with hydrogen to produce hydrocarbon fuels and chemicals. The hydrocarbon fuels produced include sustainable aviation fuel (SAP) that meets ASTM D7566 specification and diesel fuel that meets ASTM D975 specification. The hydrogen and oxygen are produced from the electrolysis of water. The carbon dioxide can be captured from industrial point sources such as power plants, ethanol plants, steel mills, or other producers of carbon dioxide. Alternatively, the carbon dioxide can be captured from the atmosphere.

Подробнее
29-08-2024 дата публикации

Thermally integrated process for the production of liquid fuels with a solid oxide electrolyzer

Номер: AU2023230619A1
Принадлежит: Infinium Technology LLC

Production of fuels from low carbon electricity and from carbon dioxide by the use of a solid oxide electrolysis cell (SOEC) and Fischer-Tropsch is shown. Fischer-Tropsch is an exothermic reaction that can be used to produce steam. Steam produced from the Liquid Fuel Production (LFP) reactor system, where the Fischer-Tropsch reaction occurs, is used as feed to the SOEC. The higher temperature steam improves the efficiency of the overall electrolysis system. The integration of the LFP steam improves the efficiency of the electrolysis because the heat of vaporization for the liquid water does not have to be supplied by the electrolyzer.

Подробнее
23-08-2024 дата публикации

Reactor catalítico para conversión de dióxido de carbono e hidrógeno en gas de síntesis

Номер: CL2024001391A1
Принадлежит: Infinium Tech Llc

La presente invención se dirige en general a un reactor para la producción de gas de síntesis bajo en carbono a partir de dióxido de carbono capturado e hidrógeno renovable. El hidrógeno se genera a partir del agua mediante un electrolizador alimentado por electricidad renovable o a partir de cualquier otro procedimiento de producción de hidrógeno con bajas emisiones de carbono. El reactor catalítico mejorado es eficiente desde el punto de vista energético y robusto cuando funciona a temperaturas de hasta 982,22 C. Las eficiencias de conversión de dióxido de carbono son superiores al 75 por ciento con una selectividad de monóxido de carbono superior al 98 por ciento. El reactor catalítico está construido con materiales que son física y químicamente robustos hasta 982,22 C. Como resultado, estos materiales no reaccionan con la mezcla de hidrógeno y dióxido de carbono ni con los productos de monóxido de carbono y vapor. Los materiales del reactor no tienen actividad catalítica ni modifican la composición física y química del catalizador de conversión. Los elementos calefactores resistivos eléctricos están integrados en el lecho catalítico del reactor de modo que la temperatura interna no disminuya más de 37,778 C desde la entrada en ningún punto del reactor. El proceso catalítico presenta una reducción del rendimiento inferior al 0,5 por ciento por cada 1.000 horas de funcionamiento.

Подробнее