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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

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Применить Всего найдено 23399. Отображено 100.
16-05-1996 дата публикации

УСТАНОВКА ДЛЯ ПРОИЗВОДСТВА ЦЕМЕНТА

Номер: RU0000002109U1

Установка для производства цемента, содержащая установленные в технологической последовательности бункеры для цементного сырья с соответствующими устройствами, обжиговую печь, холодильник, систему пылеочистки, отличающаяся тем, что обжиговая печь снабжена боковым люком загрузки твердых отходов. (19) RU (11) (13) 2 109 U1 (51) МПК C04B 7/36 (1995.01) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К СВИДЕТЕЛЬСТВУ (21), (22) Заявка: 95104448/20, 24.03.1995 (46) Опубликовано: 16.05.1996 (71) Заявитель(и): Товарищество с ограниченной ответственностью "Баргузин" (73) Патентообладатель(и): Товарищество с ограниченной ответственностью "Баргузин" U 1 2 1 0 9 R U Ñòðàíèöà: 1 U 1 (57) Формула полезной модели Установка для производства цемента, содержащая установленные в технологической последовательности бункеры для цементного сырья с соответствующими устройствами, обжиговую печь, холодильник, систему пылеочистки, отличающаяся тем, что обжиговая печь снабжена боковым люком загрузки твердых отходов. 2 1 0 9 (54) УСТАНОВКА ДЛЯ ПРОИЗВОДСТВА ЦЕМЕНТА R U (72) Автор(ы): Потехин С.Н., Савилова Г.Н. RU 2 109 U1 RU 2 109 U1 RU 2 109 U1 RU 2 109 U1

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16-07-1996 дата публикации

ЗАВОД ПО ПРОИЗВОДСТВУ ЦЕМЕНТА

Номер: RU0000002387U1

Завод по производству цемента, состоящий из ряда расположенных в технологической последовательности функциональных установок по приготовлению и обработке сырьевой смеси и соединяющих их транспортирующих устройств, отличающийся тем, что он выполнен в виде герметичного модуля с размещением в последнем указанных установок и транспортирующих устройств, причем установки помещены в герметичные корпуса или кожухи, а транспортирующие устройства - в трубопроводы, герметично соединенные с корпусами или кожухами установок. (19) RU (11) (13) 2 387 U1 (51) МПК C04B 7/36 (1995.01) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К СВИДЕТЕЛЬСТВУ (21), (22) Заявка: 95104449/20, 24.03.1995 (71) Заявитель(и): Товарищество с ограниченной ответственностью "Баргузин" (46) Опубликовано: 16.07.1996 (73) Патентообладатель(и): Товарищество с ограниченной ответственностью "Баргузин" U 1 2 3 8 7 R U Ñòðàíèöà: 1 U 1 (57) Формула полезной модели Завод по производству цемента, состоящий из ряда расположенных в технологической последовательности функциональных установок по приготовлению и обработке сырьевой смеси и соединяющих их транспортирующих устройств, отличающийся тем, что он выполнен в виде герметичного модуля с размещением в последнем указанных установок и транспортирующих устройств, причем установки помещены в герметичные корпуса или кожухи, а транспортирующие устройства - в трубопроводы, герметично соединенные с корпусами или кожухами установок. 2 3 8 7 (54) ЗАВОД ПО ПРОИЗВОДСТВУ ЦЕМЕНТА R U (72) Автор(ы): Потехин С.Н., Савилова Г.Н. RU 2 387 U1 RU 2 387 U1 RU 2 387 U1 RU 2 387 U1 RU 2 387 U1

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05-01-2012 дата публикации

Method for producing photocatalytically active clinker

Номер: US20120000395A1
Принадлежит: Holcim Technology Ltd

In a method for producing photocatalytically active clinker, TiO 2 -containing materials are reacted to calcium titanates, particularly CaTiO 3 , with clinker raw meal or clinker raw mix.

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10-02-2001 дата публикации

УСТРОЙСТВО ДЛЯ ЗАПОЛНЕНИЯ ПУСТОТ ПРИ СТРОИТЕЛЬСТВЕ И РЕМОНТЕ ИНЖЕНЕРНЫХ СООРУЖЕНИЙ

Номер: RU0000016735U1

1. Устройство для заполнения пустот при строительстве и ремонте инженерных сооружений, содержащее трубу с размещенным в ней источником радиоактивного излучения и систему подачи полимерцементной заполняющей смеси, отличающееся тем, что источник радиоактивного излучения размещен в зоне протекания потока заполняющей смеси для обеспечения возможности радиационного облучения потока, а конец трубы открыт для выхода заполняющей смеси. 2. Устройство по п.1, отличающееся тем, что источник радиоактивного излучения представляет собой управляемый генератор излучения, например, нейтронного или γ-излучения. (19) RU (11) 16 735 (13) U1 (51) МПК C04B 7/00 (2000.01) E21B 33/13 (2000.01) РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К СВИДЕТЕЛЬСТВУ (21), (22) Заявка: 2000126084/20 , 19.10.2000 (24) Дата начала отсчета срока действия патента: 19.10.2000 (46) Опубликовано: 10.02.2001 (72) Автор(ы): Вишневецкий Виктор (US) , Романский С.А.(RU), Телешов Э.Н.(RU), Громов В.Ф.(RU) (73) Патентообладатель(и): Романский Сергей Александрович (RU) U 1 1 6 7 3 5 R U Ñòðàíèöà: 1 U 1 (57) Формула полезной модели 1. Устройство для заполнения пустот при строительстве и ремонте инженерных сооружений, содержащее трубу с размещенным в ней источником радиоактивного излучения и систему подачи полимерцементной заполняющей смеси, отличающееся тем, что источник радиоактивного излучения размещен в зоне протекания потока заполняющей смеси для обеспечения возможности радиационного облучения потока, а конец трубы открыт для выхода заполняющей смеси. 2. Устройство по п.1, отличающееся тем, что источник радиоактивного излучения представляет собой управляемый генератор излучения, например, нейтронного или γ-излучения. 1 6 7 3 5 (54) УСТРОЙСТВО ДЛЯ ЗАПОЛНЕНИЯ ПУСТОТ ПРИ СТРОИТЕЛЬСТВЕ И РЕМОНТЕ ИНЖЕНЕРНЫХ СООРУЖЕНИЙ R U Адрес для переписки: 121165, Москва, а/я 15, ООО Патентно-правовая фирма "Юстис" (71) Заявитель(и): Романский Сергей Александрович (RU) U 1 U 1 1 6 7 3 5 1 6 7 3 5 ...

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27-10-2006 дата публикации

ТЕХНОЛОГИЧЕСКИЙ КОМПЛЕКС ПО ПРОИЗВОДСТВУ ЦЕМЕНТА

Номер: RU0000057741U1

Технологический комплекс по производству цемента, содержащий смонтированные в производственном промышленном здании, последовательно установленные и соединенные транспортирующими устройствами бункера для исходного материала с соответствующими питателями и дозаторами, установку для температурной обработки сырьевого компонента, измельчитель сырьевой, цементную мельницу, циклон с электрофильтрами, трубопроводом выпуска отработанных газов и конвейером возврата пылевидной фракции, цементные силосы, отличающийся тем, что в качестве сырья используют клинкер, гипс и граншлак, причем для сушки граншлака в качестве установки для температурной обработки используют сушильный барабан, а для измельчения гипса используют щековую и молотковую дробилки, кроме того, комплекс дополнительно содержит объединенный склад для сбора готовых сырьевых компонентов, установленный перед цементной мельницей, имеющей приемные бункеры с дисковыми питателями и соединенной через сосуды пневмокамерных насосов с циклоном и электрофильтрами. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 57 741 (13) U1 (51) МПК C04B 7/36 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2006122981/22 , 27.06.2006 (24) Дата начала отсчета срока действия патента: 27.06.2006 (45) Опубликовано: 27.10.2006 (72) Автор(ы): Давлетшин Эдуард Наильович (RU) (73) Патентообладатель(и): Давлетшин Эдуард Наильович (RU) R U Адрес для переписки: 423800, Республика Татарстан, г. Набережные Челны, пр-кт Вахитова, 34, кв.80, Э.Н. Давлетшину U 1 5 7 7 4 1 R U Ñòðàíèöà: 1 U 1 Формула полезной модели Технологический комплекс по производству цемента, содержащий смонтированные в производственном промышленном здании, последовательно установленные и соединенные транспортирующими устройствами бункера для исходного материала с соответствующими питателями и дозаторами, установку для температурной обработки сырьевого компонента, измельчитель сырьевой, цементную ...

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10-06-2008 дата публикации

МИНИ-ЦЕМЗАВОД

Номер: RU0000073870U1

Мини-цемзавод, содержащий ряд расположенного в технологической последовательности функционального оборудования по приготовлению и обработке сырьевой смеси, включающее питатели с приемными бункерами, сырьевую мельницу, дозаторы, печь обжига, систему очистки, цементную мельницу, накопители готовой продукции, и соединяющие оборудование транспортирующие устройства, отличающийся тем, что дополнительно содержит оборудование для сушки исходных компонентов, установленное перед оборудованием спекания, система очистки выполнена двухступенчатой, а технологическое оборудование размещено в двух связанных между собой функциональных блоках, один из которых - блок спекания клинкера - включает в себя оборудование для сушки, измельчения и спекания исходных компонентов, а другой - блок помола цемента - включает в себя оборудование для помола клинкера, инертных, активирующих и корректирующих добавок, их весового дозирования, накопители готовой продукции и расфасовки продукции в тару. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 73 870 (13) U1 (51) МПК C04B 7/36 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2007131252/22 , 16.08.2007 (24) Дата начала отсчета срока действия патента: 16.08.2007 (45) Опубликовано: 10.06.2008 (72) Автор(ы): Давлетшин Эдуард Наильович (RU) (73) Патентообладатель(и): Давлетшин Эдуард Наильович (RU) U 1 7 3 8 7 0 R U Ñòðàíèöà: 1 U 1 Формула полезной модели Мини-цемзавод, содержащий ряд расположенного в технологической последовательности функционального оборудования по приготовлению и обработке сырьевой смеси, включающее питатели с приемными бункерами, сырьевую мельницу, дозаторы, печь обжига, систему очистки, цементную мельницу, накопители готовой продукции, и соединяющие оборудование транспортирующие устройства, отличающийся тем, что дополнительно содержит оборудование для сушки исходных компонентов, установленное перед оборудованием спекания, система очистки ...

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10-08-2008 дата публикации

МЕХАНОАКТИВАТОР ЦЕМЕНТА

Номер: RU0000075386U1

1. Механоактиватор цемента, включающий корпус, станину, электродвигатель и рабочий орган, отличающийся тем, что рабочий орган выполнен в виде встречно вращающихся с одинаковой скоростью дисков, электродвигатели имеют полые валы для подачи цемента и воздуха, диски снабжены шайбами для регулирования зазора между ними, имеется система управления параметрами помола. 2. Механоактиватор по п.1, отличающийся тем, что диски могут иметь синхронные (расположенные напротив друг друга) окружные канавки овальной или круглой формы и асинхронные (расположенные со смещением относительно друг друга) окружные канавки овальной или круглой формы. 3. Механоактиватор по п.1, отличающийся тем, что диски при диаметре 1200 мм могут иметь скорость вращения 1500 об/мин. 4. Механоактиватор по п.1, отличающийся тем, что диски, с возможностью увеличения действия электростатического электричества, полностью или частично покрываются диэлектриком, например стеклом, или могут быть изготовлены из диэлектрического материала. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 75 386 (13) U1 (51) МПК C04B 7/52 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2008113090/22 , 28.03.2008 (24) Дата начала отсчета срока действия патента: 28.03.2008 (45) Опубликовано: 10.08.2008 (73) Патентообладатель(и): ОБЩЕСТВО С ОГРАНИЧЕННОЙ ОТВЕТСТВЕННОСТЬЮ "МОНОЛИТ" (RU) U 1 7 5 3 8 6 R U Ñòðàíèöà: 1 U 1 Формула полезной модели 1. Механоактиватор цемента, включающий корпус, станину, электродвигатель и рабочий орган, отличающийся тем, что рабочий орган выполнен в виде встречно вращающихся с одинаковой скоростью дисков, электродвигатели имеют полые валы для подачи цемента и воздуха, диски снабжены шайбами для регулирования зазора между ними, имеется система управления параметрами помола. 2. Механоактиватор по п.1, отличающийся тем, что диски могут иметь синхронные (расположенные напротив друг друга) окружные канавки овальной или круглой ...

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10-09-2008 дата публикации

ТЕХНОЛОГИЧЕСКАЯ ЛИНИЯ ДЛЯ ОЧИСТКИ И УТИЛИЗАЦИИ ПЫЛИ ПРИ ПРОИЗВОДСТВЕ ПОРТЛАНДЦЕМЕНТА

Номер: RU0000076021U1

Технологическая линия для очистки и утилизации пыли при производстве портландцемента, включающая емкости для приема пыли печей, соединяемые транспортерами с пневмонасосами со средствами формирования шлама, отличающаяся тем, что установка дополнительно содержит электрофильтры для вращающихся печей, шнековые транспортеры, расположенные под электрофильтрами и попарно соединенные со сборными транспортерами, конечные участки каждого из которых установлены над приемными бункерами пневмовинтовых насосов, соединенных отдельными трубопроводами пыли с общим бункером объемом не менее 10 м для приема пыли, снабженным аспиратором в виде рукавного фильтра и ячейковым питателем, обеспечивающим транспортировку пыли в смеситель, смеситель соединен посредством трубопровода пылевого шлама с насосом с накопительной емкостью для сбора шлама, содержащей приспособления для подачи в него заводского шлама, емкость для шлама посредством трубопроводов соединена с пресс-фильтрами, выполненными с возможностью очистки шлама от щелочных и хлорных соединений, пресс-фильтры снабжены трубопроводом для подачи шлама в печь. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 76 021 (13) U1 (51) МПК C04B 7/06 C04B 7/60 (2006.01) (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2008106597/22 , 22.02.2008 (24) Дата начала отсчета срока действия патента: 22.02.2008 (45) Опубликовано: 10.09.2008 Ñòðàíèöà: 1 U 1 7 6 0 2 1 R U U 1 (54) ТЕХНОЛОГИЧЕСКАЯ ЛИНИЯ ДЛЯ ОЧИСТКИ И УТИЛИЗАЦИИ ПЫЛИ ПРИ 7 6 0 2 1 (73) Патентообладатель(и): Рогачев Сергей Петрович (RU), Михин Алексей Семенович (RU), Гудков Александр Тихонович (RU), Ахмеджанов Харис Ибрагимович (RU), Ушев Алексей Иванович (RU), Фирсов Иван Иванович (RU), Бабкин Владимир Александрович (RU), Заиков Геннадий Ефремович (RU), Сизов Юрий Иванович (RU), Белоусов Сергей Петрович (RU), Рахимов Александр Имануилович (RU), Бабкин Вячеслав Михайлович (RU), Гудков Михаил Александрович ( ...

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10-11-2008 дата публикации

ЗАВОД ПО ПРОИЗВОДСТВУ ЦЕМЕНТА

Номер: RU0000077860U1

1. Завод по производству цемента, содержащий измельчитель первичного измельчения сырья, печь для получения клинкера из измельченного сырья, связанную с бункером для хранения клинкера, выход которого связан с измельчителем клинкера, отличающийся тем, что измельчитель первичного измельчения сырья выполнен в виде молотковой дробилки, причем завод снабжен последовательно соединенными друг с другом сепаратором и измельчителем, вход которого связан с выходом измельчителя первичного измельчения сырья, а выходы сепаратора связаны с печью и входом соединенного с ним измельчителя, с выходом бункера соединено несколько измельчителей клинкера, выход каждого из которых соединен со своим сепаратором, имеющим выход для выдачи готового продукта и выход, соединенный со входом своего измельчителя. 2. Завод по производству цемента по п.1, отличающийся тем, что в качестве второго измельчителя сырья использована виброимпульсная параболическая дробилка. 3. Завод по производству цемента по п.1, отличающийся тем, что в качестве измельчителей клинкера использованы виброимпульсные измельчители. 4. Завод по производству цемента по п.1, отличающийся тем, что второй измельчитель сырья, печь и измельчитель клинкера оснащены аппаратами электромагнитного воздействия на находящееся в них сырье. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 77 860 (13) U1 (51) МПК C04B 7/36 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2008119846/22 , 21.05.2008 (24) Дата начала отсчета срока действия патента: 21.05.2008 (45) Опубликовано: 10.11.2008 (73) Патентообладатель(и): Моисеев Валерий Андреевич (RU), Андриенко Владимир Георгиевич (RU), Зарогатский Леонид Петрович (RU) Ñòðàíèöà: 1 U 1 7 7 8 6 0 R U U 1 Формула полезной модели 1. Завод по производству цемента, содержащий измельчитель первичного измельчения сырья, печь для получения клинкера из измельченного сырья, связанную с бункером для хранения клинкера, выход ...

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10-11-2008 дата публикации

УСТАНОВКА ДЛЯ ДИСПЕРГИРОВАНИЯ ЦЕМЕНТНОГО КЛИНКЕРА

Номер: RU0000077861U1

Установка для диспергирования цементного клинкера, включающая печь для расплава и устройство диспергирования, отличающаяся тем, что она содержит устройство диспергирования, превращающее мельчайшие сферические капли расплава в процессе их распыления в электрическом поле с помощью двух вращающихся дисков с лопатками на периферии и неподвижного кольца, имеющего внутреннюю поверхность в виде усеченного конуса с наклонной образующей в 44-45° по отношению к вертикали, теплоизолирующего экрана, при дальнейшем охлаждении в приемной охлаждающей камере. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 77 861 (13) U1 (51) МПК C04B 7/47 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2008106263/22 , 18.02.2008 (24) Дата начала отсчета срока действия патента: 18.02.2008 (45) Опубликовано: 10.11.2008 7 7 8 6 1 R U Формула полезной модели Установка для диспергирования цементного клинкера, включающая печь для расплава и устройство диспергирования, отличающаяся тем, что она содержит устройство диспергирования, превращающее мельчайшие сферические капли расплава в процессе их распыления в электрическом поле с помощью двух вращающихся дисков с лопатками на периферии и неподвижного кольца, имеющего внутреннюю поверхность в виде усеченного конуса с наклонной образующей в 44-45° по отношению к вертикали, теплоизолирующего экрана, при дальнейшем охлаждении в приемной охлаждающей камере. Ñòðàíèöà: 1 U 1 U 1 (54) УСТАНОВКА ДЛЯ ДИСПЕРГИРОВАНИЯ ЦЕМЕНТНОГО КЛИНКЕРА 7 7 8 6 1 (73) Патентообладатель(и): Государственное образовательное учреждение высшего профессионального образования "Курский государственный технический университет" (RU) R U Адрес для переписки: 305040, г.Курск, ул. 50 лет Октября, 94, КурскГТУ, ОИС (72) Автор(ы): Голубев Михаил Николаевич (RU), Захаров Иван Сафонович (RU), Голубев Александр Михайлович (RU), Капустин Владимир Корнелиевич (RU), Шевченко Олег Ульянович (RU) U 1 U 1 7 7 8 6 1 7 7 8 ...

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27-04-2010 дата публикации

УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ПОРТЛАНДЦЕМЕНТА

Номер: RU0000093391U1

1. Установка для получения портландцемента, содержащая бункеры для помещения в них компонентов портландцемента, оснащенные на выходе дозирующими устройствами, связанными посредством элеватора с бункером для хранения усредненной смеси, измельчители усредненной смеси и бункер для хранения готовой продукции, отличающаяся тем, что в качестве измельчителей используют параболические мельницы, вход каждой из которых через дозирующее устройство связан с выходом бункера для усредненной смеси, а выходы связаны посредством элеваторов с входом пневмоклассификатора, один выход пневмоклассификатора связан с входом бункера для усредненной смеси, а другой - с бункером для готового продукта, на выходе которого установлено дозирующее устройство. 2. Установка для получения портландцемента по п.1, отличающаяся тем, что в качестве дозирующих устройств используют вибрационные дозаторы. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 93 391 (13) U1 (51) МПК C04B 7/36 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (21), (22) Заявка: 2009148961/22, 30.12.2009 (24) Дата начала отсчета срока действия патента: 30.12.2009 (45) Опубликовано: 27.04.2010 (73) Патентообладатель(и): Закрытое акционерное общество "КомпомашТЭК" (RU) U 1 9 3 3 9 1 R U Ñòðàíèöà: 1 ru CL U 1 Формула полезной модели 1. Установка для получения портландцемента, содержащая бункеры для помещения в них компонентов портландцемента, оснащенные на выходе дозирующими устройствами, связанными посредством элеватора с бункером для хранения усредненной смеси, измельчители усредненной смеси и бункер для хранения готовой продукции, отличающаяся тем, что в качестве измельчителей используют параболические мельницы, вход каждой из которых через дозирующее устройство связан с выходом бункера для усредненной смеси, а выходы связаны посредством элеваторов с входом пневмоклассификатора, один выход пневмоклассификатора связан с входом бункера для усредненной смеси, а другой - ...

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27-08-2010 дата публикации

КОМБИНИРОВАННАЯ УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ МНОГОКОМПОНЕНТНОГО ЦЕМЕНТА

Номер: RU0000097127U1

Комбинированная установка для получения многокомпонентного цемента, включающая установку для получения портландцемента, установку для обработки влажных и неабразивных материалов и установку для обработки трудноразмалываемых и абразивных компонентов цемента, причем выходы этих установок являются входами смесителя активного типа; при этом установка для получения портландцемента включает соединенные между собой ударно-отражательную дробилку, ударную роторную вертикальную дробилку, ударную дробилку с вертикальным валом, статический сепаратор или классификатор, накопительный бункер и роторный дезинтегратор-активатор; установка для обработки влажных и неабразивных материалов включает соединенные между собой молотковую сушилку-дробилку, статический сепаратор, накопительный бункер и струйную мельницу; установка для обработки трудноразмалываемых и абразивных компонентов цемента включает соединенные между собой струйную дробилку, сепаратор, бункер и активатор. Ц 97127 ко РОССИЙСКАЯ ФЕДЕРАЦИЯ 7 ВУ” 97127” 41 ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ИЗВЕЩЕНИЯ К ПАТЕНТУ НА ПОЛЕЗНУЮ МОДЕЛЬ ММ9К Досрочное прекращение действия патента из-за неуплаты в установленный срок пошлины за поддержание патента в силе Дата прекращения действия патента: 23.01.2019 Дата внесения записи в Государственный реестр: 04.12.2019 Дата публикации и номер бюллетеня: 04.12.2019 Бюл. №34 Стр.: 1 дб па П

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01-03-2019 дата публикации

Гранулятор рисовой шелухи

Номер: RU0000187319U1

Полезная модель относится к устройствам для гранулирования материалов, и может быть использована в сельскохозяйственной, строительной отраслях при производстве легкого пустотелого заполнителя для строительных материалов на основе отходов рисопереработки. Для расширения ассортимента устройств, способных производить требуемые по размеру гранулы, предлагается гранулятор рисовой шелухи, который содержит наклонный цилиндрический корпус, приводимый во вращение, с закрепленной на нем втулкой, установленный на центральном валу на двух подшипниковых опорах, закрепленных на раме. Коаксиально расположенные загрузочный патрубок с отверстиями, установленный на центральном валу с помощью двух втулок, снабженных спицами, и цилиндрическая труба, совершающая возвратно-поступательные движения посредством зубчатой передачи от электропривода, с закрепленным на ее боковой поверхности ножом. Патрубок для ввода жидких компонентов, закрепленный на раме, выгрузное отверстие, расположенное в боковой стенке наклонного цилиндрического корпуса, закрывающееся шиберной задвижкой. 2 ил. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 187 319 U1 (51) МПК B01J 2/14 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК B01J 2/14 (2018.08) (21)(22) Заявка: 2018134849, 01.10.2018 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): Общество с ограниченной ответственностью "ШелРис" (ООО "ШелРис") (RU) Дата регистрации: 01.03.2019 (56) Список документов, цитированных в отчете о поиске: RU 2475167 C1, 20.02.2013. RU 80394 U1, 10.02.2009. RU 2375188 C1, 10.12.2009. DE 10241118 A1, 18.03.2004. (45) Опубликовано: 01.03.2019 Бюл. № 7 1 8 7 3 1 9 R U (54) ГРАНУЛЯТОР РИСОВОЙ ШЕЛУХИ (57) Реферат: Полезная модель относится к устройствам для гранулирования материалов, и может быть использована в сельскохозяйственной, строительной отраслях при производстве легкого пустотелого заполнителя для строительных материалов на основе отходов ...

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26-01-2012 дата публикации

Cement compositions with a high-density additive of silicon carbide or sintered bauxite

Номер: US20120018155A1
Принадлежит: Halliburton Energy Services Inc

A method of cementing in a subterranean formation comprising the steps of: (A) introducing a cement composition into the subterranean formation, the cement composition comprising: (i) cement; (ii) water; and (iii) a high-density additive selected from the group consisting of silicon carbide, sintered bauxite, and any combination thereof, wherein the cement composition has a density of at least 16 pounds per gallon; and (B) allowing the cement composition to set. According to an embodiment, the high-density additive is in a concentration of at least 30% by weight of the cement. A cement composition for use in an oil or gas well comprises: (A) cement; (B) water; and (C) a high-density additive selected from the group consisting of silicon carbide, sintered bauxite, and a combination thereof, wherein the high-density additive is in a concentration of at least 30% by weight of the cement, and wherein the cement composition has a density of at least 16 pounds per gallon.

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09-02-2012 дата публикации

System and method for manufacturing cement clinker utilizing waste materials

Номер: US20120031307A1
Автор: John Graham Whellock
Принадлежит: Individual

Techniques are generally described for producing cement clinker that includes forming cement clinker in a kiln, heating waste additives, and applying the heated waste additives to the cement clinker in the kiln. Additionally, examples are generally described that include an apparatus for producing cement clinker that includes a kiln in which cement clinker is formed and a device having an opening positioned inside the kiln which provides heated waste additives to the kiln for application to the cement clinker. An example device for applying waste additives to cement clinker includes an eductor configured to receive waste additives and transport air in which the waste additives are pneumatically entrained, and includes a lance coupled to the eductor and configured to receive the pneumatically entrained waste additives and receive a support gas that reacts with the waste additives and heats the same for application to the cement clinker.

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16-02-2012 дата публикации

High or ultra-high performance concrete

Номер: US20120037045A1
Принадлежит: Lafarge SA

A binder premix includes from 0.2% to 63% of a material of an ultrafine particle size category, including individual particles with a D90 value less than 1 μm and/or with a BET specific surface greater than 5 m 2 /g; from 8% to 63% of selected Portland cement including particles with a D90 value less than 30 μm and from 25% to 85% of a material, other than the cement, of a fine particle size category, including particles for which the D10 and D90 values are from 1 μm to 120 μm and with a BET specific surface less than 5 m 2 /g. A binder mix including, in addition to the premix, a material of a medium particle size category, including particles for which the D10 and D90 values are from 120 μm to 5 mm is disclosed.

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16-02-2012 дата публикации

Method and Apparatus for Controlling Acid Gas Emissions from Cement Plants

Номер: US20120039778A1
Автор: James J. Schwab
Принадлежит: Envirocare International Inc

A method and apparatus for controlling emissions of acid forming gases such as sulfur dioxide from cement plants is disclosed. Gaseous effluent from the cement plant pyroprocessing chamber is routed to the plant's raw mill to heat and dry the feed meal used in cement production. When the raw mill is in operation microfine lime particles are sprayed into the raw mill using a nozzle system. The spraying of hydrated lime into the raw mill scrubs acid forming gases in the process gaseous effluent. When the raw mill is not operational, microfine lime is sprayed into a gas conditioning tower that is also used to reduce the temperature of the effluent gases to facilitate efficient collection of dust particles prior to emission of the cleansed effluent flow into the atmosphere.

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17-05-2012 дата публикации

Method and system for separating mercury from waste gases of a cement production process

Номер: US20120118151A1
Принадлежит: THYSSENKRUPP POLYSIUS AG

In the method according to the invention for separating mercury from waste gases of a cement production process, the mercury is sorbed on a sorbent, the sorbent is subsequently discharged from the process and supplied to a discharge reactor which is operated with a carrier gas. The sorbent is heated there to temperatures of more than 250° C. so that the mercury is discharged from the sorbent and changed into the gas phase, the gas of the discharge reactor that has accumulated mercury subsequently having the dust removed from it in a preliminary dust removal device, and only a part-flow of the gas which has been enriched and had the dust removed from it in this manner being drawn off at high temperatures and cleaned in a subsequent sorption stage, whilst the remaining part-flow is brought to the temperature required for the discharge of the mercury in the discharge reactor in a heat transfer system and is again supplied as a carrier gas to the discharge reactor.

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07-06-2012 дата публикации

Heavy weight concrete composition using slag byproducts

Номер: US20120137933A1
Принадлежит: Korea Railroad Research Institute KRRI

Disclosed is a heavyweight concrete composition using slag byproducts, including: ground granulated blast furnace slag; slow-cooled electric-arc-furnace oxidizing slag or atomized steel slag used as a fine aggregate; a coarse aggregate; water; and a chemical admixture based on 100 parts by weight high-early-strength cement. Thus, the heavyweight concrete composition contains a large quantity of steel slag and blast-furnace slag that are byproducts in iron-making and steel-making processes, thereby remarkably reducing an amount of emission of carbon dioxide and maximizing the recycling of waste resources for preserving the natural environment. As a result, an eco-friendly heavyweight concrete product can be made.

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14-06-2012 дата публикации

Green Cement for Sustainable Construction

Номер: US20120145043A1
Принадлежит: EMPIRE TECHNOLOGY DEVELOPMENT LLC

“Green” cements, which can be carbon neutral or negative, can be prepared at lower temperatures (450° C.-500° C.) by utilizing feed compositions comprising (i) TiO 2 , TaO x N y , TiO x N y , RuO 2 , Pt, TaO, band gap materials, or a first mixture thereof; (ii) AI 2 O 3 ; and (iii) Ca 2 SiO 2 , MgSiO 2 , MnSiO 2 , or a second mixture thereof; and spent wash with melanoidin as a binder.

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14-06-2012 дата публикации

Cementitious compositions

Номер: US20120145044A1

The invention provides a cementitious composition comprising a cement component comprising (i) an accelerant, (ii) a calcium sulphate source and (iii) an ettringite forming cement; an aggregate; and optionally water; wherein the cement has a minimum unconfined compressive strength of 1500 psi when tested in accordance with ASTM C1140 and/or C1604 at 15 minutes after placement; methods for its use and concrete formed from it.

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14-06-2012 дата публикации

Additives for a hydraulic binder based on belite-calcium-sulphoaluminate-ferrite clinker

Номер: US20120145045A1
Принадлежит: Lafarge SA

A composition includes at least, in % expressed by mass relative to the total mass of the composition, from 0.01 to 3% of polycarboxylic acid or salts thereof, the polycarboxylic acid including 2 to 4 carboxyl groups per molecule; and from 97 to 99.99% of a Belite-Calcium-Sulphoaluminate-Ferrite clinker (BCSAF clinker).

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28-06-2012 дата публикации

Process for the Manufacture of Synthetic Pozzolan

Номер: US20120160135A1
Принадлежит: FLSmidth AS

Disclosed is a process for the manufacturing of synthetic pozzolan with desirable color properties. Feed material is dried, crushed, and preheated in a drier crusher. The dry, crushed material is collected and fed to a calciner where it is heated to become a synthetic pozzolan. The synthetic pozzolan is then fed to a cooler where it is maintained for a least a portion of the cooling step in a reducing atmosphere.

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05-07-2012 дата публикации

Mixing calciner

Номер: US20120171633A1
Принадлежит: Mitsubishi Materials Corp

An object of this invention is to provide a mixing calciner that can separate and recover CO 2 gas in a high concentration, which is generated when a to-be-calcined cement material is mixed with a superheated calcined portion and calcined, by employing a fluidized-bed type or a spouted-bed type. The invention provides a mixing calciner ( 12 ) which mixes the calcined cement material with the superheated calcined portion to cause a calcination reaction, wherein the mixing calciner is the fluidized-bed type or the spouted-bed type, and is provided with a plurality of feed lines ( 25 ) for feeding the to-be-calcined cement material. In addition, this invention provides a mixing calciner which easily fluidizes or spouts a cement material even when a heat medium has a particle diameter larger than that of the cement material, and can separate and recover CO 2 gas generated in a cement-manufacturing facility in a high concentration.

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12-07-2012 дата публикации

Additive for mineral binding agents

Номер: US20120174831A1
Принадлежит: SIKA TECHNOLOGY AG

An additive composition comprising at least one lignosulfonate is used for reducing the amount of soot floating on mineral binding agents. Methods for reducing the amount of soot floating on mineral binding agents where an additive composition comprising at least one lignosulfonate is added to a mineral binding agent.

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20-09-2012 дата публикации

Hydraulic binder comprising a ground blast furnace slag

Номер: US20120234209A1
Принадлежит: Individual

The present invention concerns a hydraulic binder comprising a ground blast furnace slag in an amount comprised between 30% and 95% by mass on the binder, Portland cement clinker in an amount equal to or greater than 5% by mass on the binder, and at least one sulphate as activator, characterised in that said slag has the following properties and composition by mass: grinding fineness greater than 4000 cm2/g Blaine glass content greater than 80% SiO 2 : 30-40% Al 2 O 3 : 9-13% CaO: 34-42% with a (CaO+MgO)/(Al 2 O 3 +SiO 2 ) ratio greater than 1; and in that said sulphate is contained in a total amount, expressed as SO 3 , comprised between 0.6% and 4.5% by mass on the binder.

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13-12-2012 дата публикации

Method and device for purifying exhaust gases

Номер: US20120315205A1
Принадлежит: CHEMISCH THERMISCHE PROZESSTECHNIK GMBH

The invention relates to a regenerative thermal postcombustion plant ( 24 ) used for purifying exhaust gas comprising hydrocarbons and nitrogen oxides, particularly for exhaust gas occurring during cement clinker production, by means of which the carbon compound is oxidized and the nitrogen oxides are thermally reduced while feeding in a nitrogen-hydrogen compound at a temperature of greater than 800° C. in the multistage combustion chamber ( 35 ).

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20-12-2012 дата публикации

Cementitious foam compositions

Номер: US20120322902A1
Принадлежит: Individual

Lightweight cementitious foams of the invention have excellent dynamic and dimensional stability due to use of foaming system comprising polycarboxylate surfactant foam generating agent, foam stabilizer (e.g., PVOH), and shrinkage reducing admixture to inhibit plastic shrinkage and micro-cracking of cement. The foaming system can be used in conventional cement mortars or concretes as well as with exemplary cementitious slurry systems of the invention, which include an expansive agent, a cross-linking agent for the foam stabilizer. Microfibers can be used in the foam, slurry, or both, to prevent micro-cracking. Cementitious foams can be made without use of autoclave or lightweight aggregates to achieve enhanced compressive strength and thermal insulation properties that compare favorably with conventional foams and insulation materials at comparable densities.

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14-02-2013 дата публикации

Method and Plant For Manufacturing Cement

Номер: US20130040257A1
Принадлежит: FLSmidth AS

A method for manufacturing cement by which method cement raw materials, such as limestone and clay, are comminuted in a comminution apparatus for subsequently being heated and burned into cement clinker. The cement clinker is then cooled and directed to a comminution apparatus for comminution to cement. For some embodiments of the method, the cement raw materials and cement clinker may undergo comminution in one and the same comminution apparatus.

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25-04-2013 дата публикации

DRY MORTAR MIXTURE

Номер: US20130098271A1
Принадлежит:

A dry mortar mixture based on at least one hydraulic and/or latently hydraulic binder which in the made-up and not yet cured state has firm properties is claimed. The novel dry mortar mixture is characterized in that it contains at least one representative of a dispersant and at least one compound having superabsorbent properties. This mixture makes it possible to carry over the advantages of known tile adhesives for horizontal application to vertical application possibilities. 124-. (canceled)25. A dry mortar mixture based on at least one of a hydraulic or latently hydraulic binder , which in the made-up and fresh state has sag resistant properties , wherein the sag resistant properties are determined in accordance with DIN EN 1308 , with a Hägermann slump of <18 cm , determined in accordance with DIN EN 1015-3 , wherein it contains at least one representative of a dispersant (a) in an amount of from 0.01 to 5.0% by weight , based on the total composition of the dry mortar mixture , and a compound having superabsorbent properties (b).26. A dry mortar mixture according to claim 25 , wherein it contains a hydrophobizing agent as component (c).27. A dry mortar mixture according to claim 25 , wherein the hydraulic binder is a cement.28. A dry mortar mixture according to claim 27 , wherein the cement is selected from the group consisting of a Portland cement claim 27 , white cement claim 27 , quicklime and aluminate cement29. A dry mortar mixture according to claim 28 , wherein the Portland cement is selected from the group consisting of CEM I claim 28 , CEM II claim 28 , CEM III claim 28 , CEM IV and CEM V.30. A dry mortar mixture according to claim 27 , wherein the cement is present in an amount of from 3 to 50% by weight claim 27 , based on the total composition of the dry mortar mixture.31. A dry mortar mixture according to claim 25 , containing the latently hydraulic binder comprises at least one member selected from the group consisting of fly ash claim 25 , blast ...

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25-04-2013 дата публикации

PROCESS FOR TRANSPORTATION OF A HYDRAULIC COMPOSITION

Номер: US20130102705A1
Принадлежит: LAFARGE

A process for transportation of a fresh hydraulic composition including: 1. A process for transportation of a fresh hydraulic composition comprisingfrom 220 to 500 kg, per cubic metre of the fresh hydraulic composition, of a hydraulic binder comprising Portland cement;from 400 to 1800 kg, per cubic metre of the fresh hydraulic composition, of a sand having a D10 greater than 0.1 mm and a D90 less than 4 mm;from 150 to 1000 kg, per cubic metre of the fresh hydraulic composition, of gravel having a D10 greater than 4 mm and a D90 less than a 10 mm;from 0.05 to 5% by mass of dry extract relative to the mass of hydraulic binder, of a superplasticizer comprising a polyphosphate polyoxyalkylene polymer, a polyphosphonate polyoxyalkylene polymer, a polysulfonate polyoxyalkylene polymer or a polycarboxylate polyoxyalkylene polymer, andfrom 0.01 to 0.5% by mass of dry extract relative to the mass of hydraulic binder, of a rheology-modifying agent, different to the superplasticizer, comprising at least one compound selected from a group consisting of a viscosity-modifying agent, a water-retainer, a yield point modifier or a thixotropic agent, the process comprisingtransporting the fresh hydraulic composition for at least more than ten minutes without mixing the fresh hydraulic composition.2. The process according to claim 1 , wherein the hydraulic composition is transported in a vehicle not comprising a mixer.3. The process according to claim 1 , wherein the hydraulic composition is transported in a hermetically-sealed container.4. The process according to claim 1 , wherein the quantity of the rheology-modifying agent is from 0.01 to 2% by mass of dry extract relative to the mass of the hydraulic binder.5. The process according to claim 1 , wherein the quantity of the superplasticizer is from 0.05 to 1% by mass of dry extract relative to the mass of the hydraulic binder.6. The process according to claim 1 , wherein the hydraulic composition further comprises 0.1 to 5% by mass ...

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09-05-2013 дата публикации

METHOD FOR PRODUCING HYDRAULIC POWDER

Номер: US20130112113A1
Принадлежит: KAO CORPORATION

The present invention provides the production of the hydraulic powder containing CA in an amount of 0.5 to 9.5% by weight through a step of grinding a hydraulic compound in the presence of the alkanolamine having a freezing point of not higher than 0° C. 1. A method for producing a hydraulic powder comprising CA in an amount of 0.5 to 9.5% by weight , comprising a step of grinding a hydraulic compound in the presence of an alkanolamine having a freezing point of not higher than 0° C.2. The method for producing a hydraulic powder according to claim 1 , wherein the alkanolamine has a freezing point of not lower than −100° C.3. The method for producing a hydraulic powder according to claim 1 , wherein the alkanolamine is an alkyldiethanolamine having a linear alkyl group having 1 to 4 carbon atoms.4. The method for producing a hydraulic powder according to claim 1 , wherein the alkanolamine is N-methyldiethanolamine.5. The method for producing a hydraulic powder according to claim 1 , wherein the amount of the alkanolamine is 0.001 to 0.2 parts by weight to 100 parts by weight of the hydraulic compound.6. The method for producing a hydraulic powder according to claim 1 , wherein the alkanolamine is present in the form of an aqueous solution and the amount of water of the aqueous solution is 0.001 to 0.1 part by weight to 100 parts by weight of the hydraulic compound.7. The method for producing a hydraulic powder according to claim 1 , wherein the hydraulic powder contains CAF in an amount of not more than 11% by weight.8. The method for producing a hydraulic powder according to claim 1 , further using an acid.9. The method for producing a hydraulic powder according to claim 3 , further using a polyol having 3 to 8 carbon atoms.10. The method for producing a hydraulic powder according to claim 9 , wherein the polyol is one or more compounds selected from the group consisting of diethylene glycol claim 9 , glycerol claim 9 , diglycerol claim 9 , and glycerol-ethylene ...

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16-05-2013 дата публикации

Cement Accelerator

Номер: US20130118381A1
Принадлежит:

The invention relates to an inorganic binder system comprising a) calcium silicate cement, b) calcium aluminate cement, c) at least one trifunctional polyalkylene glycol and d) optionally calcium sulphate. Additionally disclosed is the use of at least one polyalkylene glycol as an accelerator for an inorganic binder system comprising a) calcium silicate cement, b) calcium aluminate cement and d) optionally calcium sulphate. 1. Inorganic binder system comprisinga) calcium silicate cementb) calcium aluminate cementc) at least one trifunctional polyalkylene glycol, andd) optionally calcium sulphate.2. Inorganic binder system according to claim 1 , wherein it comprisesa) Portland cementb) alumina cementc) at least one trifunctional polyalkylene glycol, andd) optionally anhydrite.3. Inorganic binder system according to claim 1 , wherein it comprisesa) 10 to 30% by weight of Portland cementb) 1 to 10% by weight of alumina cementc) 0.05 to 5% by weight of at least one trifunctional polyalkylene glycol based on trimethylolpropane or glycerol and polyethylene glycol, polypropylene glycol and/or polytetramethylenglycol, andd) 0 to 20% by weight of anhydrite.5. Inorganic binder system according to claim 1 , wherein the inorganic binder system is a dry mix mortar.6. Inorganic binder system according to claim 1 , wherein at least one further additive from the group of plasticizers claim 1 , redispersible polymer powders claim 1 , defoamers claim 1 , stabilizers claim 1 , water retention aids claim 1 , thickeners. dedusting agents claim 1 , accelerators claim 1 , retardants and/or pigments is present.7. Inorganic binder system according to claim 6 , wherein the further accelerators or retardants used are hydroxides claim 6 , inorganic and/or organic acids and/or salts thereof claim 6 , and/or alkali metal carbonates claim 6 , or mixtures of these compounds.8. Inorganic binder system according to claim 6 , wherein the further accelerators or retardants used are calcium hydroxide ...

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16-05-2013 дата публикации

HYDRAULIC COMPOSITION

Номер: US20130123392A1
Принадлежит: LAFARGE

A hydraulic composition including 1. A hydraulic composition comprising:from 220 to 500 kg, per cubic metre of fresh hydraulic composition, of a hydraulic binder comprising Portland cement;from 400 to 1800 kg, per cubic metre of fresh hydraulic composition, of a sand having a D10 greater than 0.1 mm and a D90 less than 4 mm;from 0.1 to 5% by mass of dry extract relative to the mass of hydraulic binder, of a retarding agent comprising a carboxylic acid, a phosphonic acid or salts thereof;from 0.05 to 5% by mass of dry extract relative to the mass of hydraulic binder, of a superplasticizer comprising a polyphosphate polyoxyalkylene polymer, a polyphosphonate polyoxyalkylene polymer, a polysulfonate polyoxyalkylene polymer or a polycarboxylate polyoxyalkylene polymer, andfrom 0.01 to 2% by mass of dry extract relative to the mass of hydraulic binder, of a rheology-modifying agent comprising at least one compound selected from a group consisting of a viscosity-modifying agent, a water-retainer, a yield point modifier or a thixotropic agent,wherein a setting time of the hydraulic composition is greater than or equal to 12 hours without triggering the setting of the hydraulic composition and a variation of the slump of the hydraulic composition, measured according to the EN 12350-2 Standard, is less than 50 mm or thea variation of the spread of the hydraulic composition, measured with a cone according to the EN 12350-2 Standard, is less than 100 mm for at least 12 hours without triggering the setting of the hydraulic composition.2. The hydraulic composition according to claim 1 , wherein the retarding agent comprises a hydroxycarboxylic acid or a salt of hydroxycarboxylic acid.3. The hydraulic composition according to claim 2 , wherein the retarding agent comprises a gluconate.4. The hydraulic composition according to claim 1 , wherein the quantity of retarding agent is comprised from 0.1 to 1% by mass of dry extract relative to the mass of the hydraulic binder.5. The ...

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30-05-2013 дата публикации

NON-CHEMICAL AIR ENTRAINED ADMIX

Номер: US20130133553A1
Автор: FERNALD MARK R.
Принадлежит: CIDRA CORPORATE SERVICES INC.

An improved concrete is provided having a concrete formed from a wet concrete mixture; and a non-chemical admix added to the wet concrete mixture and configured to contain bubbles in order to control the amount of entrained air formed in the concrete when the wet concrete mixture cures into the improved concrete. The non-chemical admix includes a multiplicity of hollow objects, bodies, elements or structures, each configured with a respective cavity, unfilled space, or hole to trap and maintain a bubble inside. The hollow objects, bodies, elements or structures include hollow cylinders, or spheres, or capillary tubes, or some combination thereof. Each hollow object, body, element or structure is configured with a dimension so as not to absorb liquid, including water, including where the dimension is in a range of about 20-30 microns, and is made of glass or a glass-like material. 1. An improved concrete comprising:a concrete formed from a wet concrete mixture; anda non-chemical admix added to the wet concrete mixture and configured to contain bubbles in order to control the amount of entrained air formed in the concrete when the wet concrete mixture cures into the improved concrete.2. An improved concrete according to claim 1 , wherein the non-chemical admix comprises a multiplicity of hollow objects claim 1 , bodies claim 1 , elements or structures claim 1 , each configured with a respective cavity claim 1 , unfilled space claim 1 , or hole to trap and maintain a bubble inside.3. An improved concrete according to claim 2 , wherein the hollow objects claim 2 , bodies claim 2 , elements or structures comprise hollow cylinders claim 2 , or spheres claim 2 , or capillary tubes claim 2 , or some combination thereof.4. An improved concrete according to claim 2 , wherein each hollow object claim 2 , body claim 2 , element or structure is configured with a dimension so as not to absorb liquid claim 2 , including water claim 2 , including where the dimension is in a range ...

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06-06-2013 дата публикации

CEMENTITIOUS BINDERS AND WOOD PARTICLES-BASED INCOMBUSTIBLE COLOURED COMPOSITE PANEL WITH STRUCTURAL HIGH PERFORMANCE

Номер: US20130139731A1

This invention relates to a composite panel made from wood and cementitious binders, with flat surfaces and several possible colours. The said panel comprises 35 to 85% of grey or white Portland cement; 10 to 30% of debarked resinous wood particles; 5 to 20% of semi-hydrated calcium sulphate; 0 to 10% of a surface accelerator; 0 to 10% of aluminium sulphate solution; 0 to 30% of calcium carbonate; and 0 to 15% of pigments. The invention uses the process of preparation for the existing VIROC panel, adjusting it to the new material. This panel, in addition to being very resistant and showing high performances in terms of resistance to impact, humidity, temperature variation, noise and fungi, as well as other microorganisms, also complies with all the requirements of the associated product standard. 1. Incombustible composite panel of high performance , made from Portland cement , gypsum and wood particles , characterized in that it comprises in weight percentage of the components with reference to the dry weight of the composition:1) 35 to 85% of grey or white Portland cement;2) 10 to 30% of debarked resinous wood particles;3) 5 to 20% of semi-hydrated calcium sulphate;4) 0 to 10% of a surface accelerator;5) 0 to 10% of aluminium sulphate solution;6) 0 to 30% of calcium carbonate; and7) 0 to 15% of pigments.2. Composite panel according to claim 1 , characterized in that the resinous wood used in order to obtain the component 2) is pinewood.3. Composite panel according to or claim 1 , characterized in that the wood particles used as the component 2) are in the form of chips.4. Composite panel according to claim 3 , characterized in that the thickness of the said chips ranges from 0.25 to 0.32 mm.5. Composite panel according to or claim 3 , characterized in that 50 to 70% of the said chips are <1 mm long and 26 to 40% have a length of 1 to 4 mm.6. Composite panel according to any of the to claim 3 , characterized in that the surface accelerator used as the component 4) ...

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06-06-2013 дата публикации

ROOFING TILE WITH ENHANCED SURFACE DURABILITY AND PROCESSES FOR MANUFACTURING THE ROOLING TILE

Номер: US20130143036A1
Принадлежит:

A new roofing tile with enhanced surface durability and processes for manufacturing the same. The abstract of the disclosure is submitted herewith as required by 37 C.F.R. §1.72(b). As stated in 37 C.F.R. §1.72(b): A brief abstract of the technical disclosure in the specification must commence on a separate sheet, preferably following the claims, under the heading “Abstract of the Disclosure.” The purpose of the abstract is to enable the Patent and Trademark Office and the public generally to determine quickly from a cursory inspection the nature and gist of the technical disclosure. The abstract shall not be used for interpreting the scope of the claims. Therefore, any statements made relating to the abstract are not intended to limit the claims in any manner and should not be interpreted as limiting the claims in any manner. 1. A method of manufacturing a coated cement roofing tile; said coated cement roofing tile comprising: a cement roofing tile substrate with a coating disposed on said cement roofing tile substrate; said coating being configured to maximize surface durability during weathering , maximize surface smoothness during weathering , and maximize surface acid-erosion resistance during weathering; providing a cement roofing tile substrate;', at least about sixty percent by weight of a material comprising calcium aluminate; and', 'no more than about one percent by weight of a sulfate;, 'mixing water and a cementitious mixture to form a cementitious slurry; said cementitious slurry comprising a hydraulic binder; said hydraulic binder comprising, 'applying said cementitious slurry to said cement roofing tile substrate and forming a cementitious coating on said cement roofing tile substrate;', 'hydrating said cementitious coating on said cement roofing tile substrate to form a coated cement roofing tile; and', 'hardening said cementitious coating to form an at least partially finished cement roofing tile., 'said method comprising the steps of2. The method ...

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13-06-2013 дата публикации

Low Embodied Energy Wallboards and Methods of Making Same

Номер: US20130145969A1
Принадлежит: Serious Energy Inc

Wallboards, as well as other building materials, are produced by methods which use significantly reduced embodied energy, generating far less greenhouse gases when compared with the energy used to fabricate gypsum wallboard. A novel cementitious core, consisting in one embodiment of post-industrial waste such as slag and combined with pH modifiers, provides a controlled exothermic reaction to create a gypsum-wallboard-like core which can be wrapped in a selected material such as recycled paper and manufactured on a conveyor system to appear, weigh and handle similar to gypsum wallboard, but without the large amounts of energy required to make gypsum wallboard. The manufacturing process results in lower greenhouse gas emissions than the processes used to make gypsum wallboard.

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20-06-2013 дата публикации

METHOD FOR PRODUCING A CLINKER FOR HYDRAULIC CEMENT WITH LOW CO2 EMISSION AND HIGH RESISTANCE

Номер: US20130152825A1
Принадлежит: CEMEX RESEARCH GROUP AG

A method for producing a clinker for cement, comprising grinding a raw flour comprising, especially, AlO, FeOand SOin contents such that the formula for calculating SOcontent of=0.261×AlO−0.638×FeO+k, where 2.5 Подробнее

20-06-2013 дата публикации

Process for utilizing organic waste materials

Номер: US20130152826A1
Автор: Cruz Armando, Stoffel Beat
Принадлежит: Holcim Technology Ltd

In a process for utilizing organic waste materials, in particular cellulose-containing, moist, organic waste materials, in a clinker production process in which the waste materials are introduced as fuel and burnt in the clinker production process, the waste materials are brought into contact with the hot exhaust gases of the clinker production process and dried in a drying step flowing in parallel therewith before they are introduced into the clinker production process. The drying step is carried out in a drying reactor in which the moist waste materials are passed together with the hot exhaust gases through a series of concentrically arranged tubes, with multiple changes in flow direction about 180°, and the temperature of the hot exhaust gases is set to a maximum value of 400° C. by mixing in of ambient air and/or air from the clinker production process before the drying step. (FIG. ) 1. A process for utilizing organic waste materials , in particular cellulose-containing , moist , organic waste materials , in a clinker production process in which the waste materials are introduced as fuel and burnt in the clinker production process , wherein the waste materials are brought into contact with the hot exhaust gases of the clinker production process and dried in a drying step flowing in parallel therewith before they are introduced into the clinker production process , characterised in that the drying step is carried out in a drying reactor in which the moist waste materials are passed together with the hot exhaust gases through a series of concentrically arranged tubes , with multiple changes in flow direction about 180° , and the temperature of the hot exhaust gases is set to a maximum value of 400° C. by mixing in ambient air and/or air from the clinker production process before the drying process.2. The process according to claim 1 , characterised in that the exhaust gases from the clinker cooler and/or the preheater are used as the hot exhaust gases.3. The ...

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27-06-2013 дата публикации

Lactate activated cement and activator compositions

Номер: US20130160678A1
Принадлежит: Glenn Schumacher, Rajeshkumar Patel

Cementitious compositions in which the cementitious properties of fly ash are carefully controlled are described. The cementitious compositions may be substantially free harsh acids and bases such as citric acids (≈pH 2.2) and alkali metal activators including alkali hydroxides (≈pH 12-14) and metal carbonates (≈pH 11.6). The use of these harsh chemicals creates acid base reactions during use of the products. Instead of these harsh chemicals, a lactic acid salt based activator is be used as a reaction accelerator. Boric compounds may be used as a retarder in the compositions.

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04-07-2013 дата публикации

METHOD FOR MANUFACTURING PLATE INORGANIC NONMETAL MATERIAL USING MOLTEN SLAG

Номер: US20130167586A1
Принадлежит: SHANDONG COKING GROUP CO., LTD.

A method for manufacturing a plate inorganic nonmetal material by using a molten slag by introducing the molten slag into a pool for preserving heat and modifying, wherein a temperature of the molten slag is 1450° C.-1600° C., and modifying a viscosity and/or a color of the molten slag according to requirements of the product manufactured. The modified molten slag is introduced into a float process furnace using tin or tin alloy carrier forming a plate of inorganic nonmetal material which is discharged at 1000-1300° C. The plate is maintained at 600° C.-900° C. for 0.5-2 hours in a non-reducing atmosphere, and then cooled to a room temperature within 1-2 hours. An energy-saving and efficient method for comprehensively utilizing the blast furnace slag is provided. The produced plate inorganic nonmetal material has such characteristics as stable color quality, abrasion resistance, pressure resistance, strong adhesiveness, low coefficient of expansion and low shrinkage ratio. 1. A method for manufacturing a plate inorganic nonmetal material by using a molten slag , comprising:introducing the molten slag into a pool for preserving heat and modifying, wherein a temperature of the molten slag is maintained at 1450° C.-1600° C., and modifying a viscosity and/or a color of the molten slag according to requirements of a product to be manufactured;introducing the modified molten slag into a float process furnace using tin or tin alloy as a carrier and preparing the plate inorganic nonmetal material from the modified molten slag, and discharging the plate inorganic nonmetal material at 1000-1300° C.; andmaintaining the plate inorganic nonmetal material at 600° C.-900° C. for 0.5-2 hours in a non-reducing atmosphere, and then gradually cooling the plate inorganic nonmetal material to a room temperature within 1-2 hours,{'sub': 2', '3', '2', '2, 'wherein the molten slag includes 10-40 wt % of AlO, 5-25 wt % of MgO, 10-50 wt % of SiO, 10-40 wt % of CaO, 0.1-5 wt % of TiO, 0.1-5 ...

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01-08-2013 дата публикации

NARROW PSD HYDRAULIC CEMENT, CEMENT-SCM BLENDS, AND METHODS FOR MAKING SAME

Номер: US20130192493A1
Принадлежит: ROMAN CEMENT LLC

Hydraulic cements, such as Portland cements and other cements that include substantial quantities of tricalcium silicate (CS), dicalcium silicate (CS), tricalcium aluminate (CA), and/or tetracalcalcium alumino-ferrite (CAF), are particle size optimized to have increased reactivity compared to cements of similar chemistry and/or decreased water demand compared to cements of similar fineness. Increasing hydraulic cement reactivity increases early strength development and release of reactive calcium hydroxide, both of which enhance SCM replacement and 1-28 day strengths compared to blends of conventional Portland cement and one or more SCMs, such as coal ash, slag or natural pozzolan. Decreasing the water demand can improve strength by decreasing the water-to-cement ratio for a given workability. The narrow PSD cements are well suited for making blended cements, including binary, ternary and quaternary blends. 1. A cement-SCM composition , comprising:a cement fraction that provides hydraulic cement particles with a d90 in a range of 11 μm to 30 μm, a d10 equal to or greater than 2 μm, and a ratio d90/d10 of less than or equal to 14.5;a coarse SCM fraction that provides coarse SCM particles with an average particle size that is about 1.25 times to about 25 times greater than an average particle size of the hydraulic cement particles and so that greater than 50% of particles larger than 20 μm provided by the coarse SCM fraction and the cement fraction comprise the coarse SCM particles; andan ultrafine SCM fraction that provides ultrafine SCM particles with a particle size so that at least 50% of particles smaller than 3 μm provided by the ultrafine SCM fraction and the cement fraction comprise the ultrafine SCM particles.2. A cement-SCM composition as in claim 1 , wherein the cement fraction comprises one or more minerals that claim 1 , when mixed with water claim 1 , react to form a cementitious binder comprised of at least one of calcium silicate hydrates or calcium ...

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01-08-2013 дата публикации

TREATMENT DEVICE AND TREATMENT METHOD FOR CHLORINE BYPASS DUST

Номер: US20130192497A1
Принадлежит: TAIHEIYO CEMENT CORPORATION

In accordance with the present invention, there is provided a treat chlorine bypass dust while preventing increases in chemical cost and concentrations of heavy metals in clinker, and ensuring stability in quality of cement. In a chlorine bypass facility extracting a part G of combustion gas, while cooling it, from a kiln exhaust gas passage, which runs from an inlet end of a cement kiln to a bottom cyclone, and recovering a high chlorine concentration chlorine bypass dust D from the extracted gas G, a slurry S containing chlorine bypass dust and SO2 gas or/and CO2 gas are contacted with each other to obtain solid content. The slurry containing chlorine bypass dust and an exhaust gas from the chlorine bypass facility or/and the exhaust gas from the cement kiln can be contacted with each other, and the solid content can be fed to a cement finishing process, which allows cement with low CaO and Ca(OH)2 contents and with stable property such as setting time to be produced. 1. A method of treating chlorine bypass dust characterized by , in a chlorine bypass facility extracting a part of combustion gas , while cooling it , from a kiln exhaust gas passage , which runs from an inlet end of a cement kite to a bottom cyclone , and recovering a high chlorine concentration chlorine bypass dust from the extracted gas , obtaining solid content by contacting a slurry containing the chlorine bypass dust and SOgas or/and COgas with each other , and determining time for reacting the slurry containing the chlorine bypass dust to the SOgas or/and the COgas by at least one selected from the group consisting of: rate of decrease in the SOgas or/and the COgas when obtaining the solid content; pH of the slurry after being reacted with the SOgas or/and the COgas , and chemical analysis value of the chlorine bypass dust.2. The method of treating chlorine bypass dust as claimed in claim 1 , wherein said slurry containing chlorine bypass dust and an exhaust gas irons the chlorine bypass ...

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08-08-2013 дата публикации

PULVERULENT MORTAR COMPOSITION HAVING IMPROVED ADHESION

Номер: US20130203899A1
Принадлежит: BOSTIK S.A.

Pulverulent mortar composition comprising a mineral binder, an inert material in the form of aggregate capable of being agglomerated in aqueous phase by means of said binder, and 0.2 to 1% of a fluid additive comprising 25 to 100% of a linear or branched, saturated or unsaturated hydrocarbon compound (i) which is liquid at room temperature and which includes one or more —COO— ester groups, the total weight of which, relative to the molar mass of said compound, is between 20 and 50%. Use for preparing an adhesive mortar for fixing ceramic tiles. 1. A pulverulent mortar composition which comprises:from 10% to 60% of an inorganic binder,from 40% to 90% of an inert material in granule form that can be agglomerated in aqueous phase by means of said binder,from 0.2% to 1% of a fluid additive comprising from 25% to 100% of a saturated or unsaturated, linear or branched hydrocarbon compound (i) which is liquid at ambient temperature and which includes one or more ester groups —COO— of which the total weight, relative to the molar mass of said compound (i), is between 20% and 50%.2. The pulverulent mortar composition as claimed in claim 1 , characterized in that cement is used as inorganic binder and sand is used as granules of inert material.3. The pulverulent mortar composition as claimed in claim 1 , characterized in that the compound (i) is a mono- claim 1 , di- claim 1 , tri- or tetra-ester.5. The pulverulent mortar composition as claimed in claim 1 , characterized in that the polar organic compound (i) includes one or more ester groups for a total weight of between 30% and 50%.6. The pulverulent mortar composition as claimed in claim 1 , characterized in that the fluid additive further comprises from 0% to 75% of an apolar organic compound (ii) which is liquid at ambient temperature.7. The pulverulent mortar composition as claimed in claim 6 , characterized in that the compound (ii) is selected from mineral oils claim 6 , paraffinic oils claim 6 , polyolefins claim 6 , ...

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15-08-2013 дата публикации

METHOD FOR RECYCLING WASTE WATER FROM A STAINLESS STEEL SLAG TREATMENT PROCESS

Номер: US20130206041A1
Принадлежит:

The present invention relates to a method for recycling waste water from a stainless steel slag treatment process wherein stainless steel slag is brought into contact with water, in particular to neutralize the free lime contained therein, thereby producing said waste water. This waste water contains heavy metals, including at least chromium, and has a pH higher than or equal to 11. In accordance with the invention, it is used as production water for manufacturing mortar and/or concrete. In this way, the heavy metals, which are dissolved in the waste water and thus readily available, become bound in the newly formed cement phases so that they are prevented from leaching. Moreover, it has been found that the workability of the fresh mortar or concrete and also the quality of the final mortar or concrete materials is not negatively affected by the use of this alkaline waste water and that an accelerated setting could be achieved during the first hours. 1. A method for recycling waste water from a stainless steel slag treatment process wherein stainless steel slag is brought into contact with water thereby producing said waste water which contains heavy metals , including at least chromium , characterised in that said waste water is used for manufacturing mortar and/or concrete , which mortar and/or concrete made by mixing at least one hydraulic binding agent , at least one aggregate and water.2. A method according to claim 1 , characterised in that the waste water used to manufacture said mortar and/or concrete has a pH higher than 7 claim 1 , in particular higher than 9 claim 1 , more particularly higher than 11 and even more particularly higher than 12.3. A method according to claim 1 , characterised in that said hydraulic binding agent contains di- and tricalcium silicates.4. A method according to claim 3 , characterised in that said hydraulic binding agent comprises Portland clinker.5. A method according to claim 4 , characterised in that said hydraulic binding ...

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15-08-2013 дата публикации

DRY GRANULATION OF METALLURGICAL SLAG

Номер: US20130206875A1
Принадлежит: PAUL WURTH S.A.

A process for dry granulation of hot liquid slag wherein the hot liquid slag is mixed with solid metallic particles so as to form a solidified, vitrified slag cake mixed with the metallic particles, the slag cake is crushed so as to form hot slag particles and heated solid particles, said particles are cooled and said solid metallic particles are recycled. 1. A process for dry granulation of hot liquid slag wherein the hot liquid slag is mixed with solid metallic particles so as to form a solidified , vitrified slag cake mixed with said metallic particles , said slag cake is crushed so as to form hot slag particles and heated solid particles , said particles are cooled and said solid metallic particles are recycled.2. The process for dry granulation of hot liquid slag according to claim 1 , wherein the hot liquid slag is poured first into a trough and then the solid metallic particles are poured into the trough containing the hot liquid slag and mixed with solid metallic particles so as to form a solidified claim 1 , vitrified slag cake.3. The process for dry granulation of hot liquid slag according to claim 2 , wherein the trough in which the hot liquid slag and the solid metallic particles are poured is integrated in a troughed belt conveyor or on a rotating drum.4. The process for dry granulation of hot liquid slag according to claim 1 , wherein said solid metallic particles have a density of at least 2.5-g/cm.5. The process for dry granulation of hot liquid slag according to claim 1 , wherein said solid metallic particles are spherical.6. The process for dry granulation of hot liquid slag according to claim 1 , wherein said solid metallic particles have a diameter of at least 2 mm.7. The process for dry granulation of hot liquid slag according to claim 1 , wherein said solid metallic particles have a diameter of less than 80 mm.8. The process for dry granulation of hot liquid slag according to claim 1 , wherein said solid metallic particles are made of a metal ...

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22-08-2013 дата публикации

Cement composition, method for producing mixed material, and method for producing cement composition

Номер: US20130213274A1
Принадлежит: Obayashi Corp

The present invention provides cement composition including 100 parts by weight of binder (B) including, 5-30 parts by weight of cement, 0-20 parts by weight of silica fume, 0-50 parts by weight of fly ash, and 42-75 parts by weight of blast furnace slag; water (W) equivalent to 80-185 kg/m 3 of water content per unit volume of concrete; aggregate (A); and chemical admixture for concrete (AD).

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22-08-2013 дата публикации

INTERNALLY CURING CEMENT BASED MATERIALS

Номер: US20130213276A1
Принадлежит: WEYERHAEUSER NR COMPANY

A method of curing cementitious material comprising added a carboxylated bleached wood pulp fiber to the material during mixing. The fiber has a carboxyl content of from 10 to 70 meq/100 g cellulose fiber. The fibers are 0.1 to 5% by weight of the dry weight of the cementitious material. The structure produced by the method. The autognous shrinkage of the cementitious material is reduced. 1. A cured cementitious structure comprisingcementitious material wherein the cementitious material is cement, andcarboxylated bleached cellulosic wood pulp fibers, the fibers having a carboxyl content of 10 to 70 meq/100 g of cellulose fiber, the fibers are 0.1 to 5% by weight of the dry weight of the cementitious material.2. The cementitious structure of wherein the fibers have a carboxyl content of 20 to 60 meq/100 g of cellulose fiber.3. The cementitious structure of wherein the fibers have a carboxyl content of 30 to 50 meq/100 g of cellulose fiber.4. The cementitious structure of wherein the fibers have a carboxyl content of 35 to 45 meq/100 g of cellulose fiber.5. The cementitious structure of wherein the fibers are 0.25 to 0.75% by weight of the dry weight of the cementitious material.6. The cementitious structure of wherein the cementitious material further comprises aggregate material.7. The cementitious structure of wherein the fibers have a carboxyl content of 20 to 60 meq/100 g of cellulose fiber.8. The cementitious structure of wherein the fibers have a carboxyl content of 30 to 50 meq/100 g of cellulose fiber.9. The cementitious structure of wherein the fibers have a carboxyl content of 35 to 45 meq/100 g of cellulose fiber.10. The cementitious structure of wherein the fibers are 0.25 to 0.75% of the dry weight of the cementitious material. This is a divisional application that claims priority under 35 U.S.C. §121 based on U.S. nonprovisional application Ser. No. 12/892,239 filed Sep. 28, 2010.The present invention relates generally to methods of and materials for ...

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05-09-2013 дата публикации

Process for controlling a crystal form of alite in portland cement clinker

Номер: US20130228102A1
Принадлежит: NANJING TECH UNIVERSITY

The present invention relates to a process of controlling crystal form of Alite in Portland cement clinker, wherein the said Portland cement clinker is thermally treated in order to change the crystal form of Alite in Portland cement clinker, so as to improve performance of resulting Portland cement clinker. The said process of present invention is easy and feasible.

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12-09-2013 дата публикации

HIGH PERFORMANCE SULFO-ALUMINOUS CLINKER

Номер: US20130233207A1
Принадлежит:

The invention relates to a sulfo-aluminous clinker with optimal setting time and short term compressive strengths, comprising a mixture of the following phases: calcium sulfoaluminate, or CA$, in amounts higher than 50% by weight of the mixture, belite, or CS, in amounts between 2 and 23%, 3CS 3C$ CaX, X being fluorine or chlorine, between 3 and 15% CACaX, X being fluorine or chlorine, between 2 and 12%, both fluorine and chlorine being altogether present in the mixture, and phase CS$ being absent. The invention also relates to a method for preparing this sulfo-aluminous clinker, and hydraulic binders comprising this clinker. 118-. (canceled)19. A sulfo-aluminous clinker comprising a mixture of:{'sub': 4', '3, '(i) calcium sulfoaluminate (CA$), in an amount greater than 50% by weight of said mixture,'}{'sub': '2', '(ii) belite (CS) in an amount ranging from 2% to 23% by weight of said mixture;'}{'sub': 2', '2, '(iii) 3CS3C$CaX, wherein X is fluorine or chlorine, in an amount ranging from 3% to 15% by weight of said mixture; and'}(iv) C11A7CaX2, wherein X is fluorine or chlorine, in an amount ranging from 2% to 12% by weight of said mixture;{'sub': 5', '2, 'wherein both fluorine and chlorine are present in said mixture, and CS$ is absent therefrom.'}20. The sulfo-aluminous clinker of claim 19 , comprising 3CS3C$CaFand CACaCl.21. The sulfo-aluminous clinker of claim 20 , further comprising CACaF.22. The sulfo-aluminous clinker of claim 19 , wherein said total combined amount of 3C$3C$CaXand CACaXis from 5% to 25% of said mixture.23. The sulfo-aluminous clinker of claim 19 , comprising from 0.01 to 10% by weight of at least one of: calcium sulfate or anhydrite (C$) claim 19 , a calcium aluminate (CA claim 19 , CA claim 19 , CAt) claim 19 , gehlenite (CAS) claim 19 , perovskite (CT) claim 19 , calcium iron titanate (CFT) claim 19 , merwinite (CMS) claim 19 , periclase claim 19 , free lime claim 19 , or ferrite (CAF or CF).24. The sulfo-aluminous clinker according to ...

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26-09-2013 дата публикации

CEMENT ADMIXTURE, CEMENT COMPOSITION, AND METHOD FOR REDUCING HEXAVALENT CHROMIUM USING THE SAME

Номер: US20130247796A1
Принадлежит: DENKI KAGAKU KOGYO KABUSHIKI KAISHA

The invention provides a cement admixture that improves the ability of concrete to bring about high initial strength, works in favor of enhancing the effect on hexavalent chromium reductions, and is less likely to decrease in the effect on hexavalent chromium reductions even upon storage as well as a method for reducing hexavalent chromium. The invention is embodied as (1) A cement admixture, characterized by comprising an expanding material containing free lime, a hydraulic compound and calcium sulfate anhydrite, and a tin sulfate-containing substance; (2) The cement admixture according to (1), characterized in that the tin sulfate-containing substance is contained in an amount of 0.2 to 8 parts by mass—as calculated on a tin sulfate basis—in a total of 100 parts by mass of the expanding material and the tin sulfate-containing substance; (3) The cement admixture according to (1) or (2), characterized in that the expanding material has been treated with carbon dioxide gas to form calcium carbonate therein; (4) The cement admixture according to any one of (1) to (3), characterized in that the expanding material has been surface treated with a shrinkage reducer; (5) A cement composition, characterized by containing cement, and the cement admixture according to any one of (1) to (4); and (6) A method for reducing hexavalent chromium, characterized by use of the cement composition according to (5). 1. A cement admixture , characterized by comprising an expanding material containing free lime , a hydraulic compound and calcium sulfate anhydrite , and a tin sulfate-containing substance.2. The cement admixture according to claim 1 , characterized in that said tin sulfate-containing substance is contained in an amount of 0.2 to 8 parts by mass—as calculated on a tin sulfate basis—in a total of 100 parts by mass of said expanding material and said tin sulfate-containing substance.3. The cement admixture according to claim 1 , characterized in that said expanding material has ...

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03-10-2013 дата публикации

CEMENT AND CONCRETE WITH CALCIUM ALUMINATES

Номер: US20130255542A1
Принадлежит: CALERA CORPORATION

Provided herein are systems, methods, and compositions related to mixtures of calcium aluminate cements with compositions comprising carbonate. The compositions comprising carbonates may be formed by sequestering carbon dioxide. 1. A cementitious composition , comprising: calcium aluminate cement (CAC) and a composition comprising carbonate wherein the composition comprising carbonate comprises a metastable component selected from the group consisting of vaterite , amorphous calcium carbonate , and combination thereof.2. The cementitious composition of claim 1 , wherein the composition comprising carbonate comprises or has at least one of the following:a) at least 50 wt % vaterite;{'sup': '13', 'b) a δC value less than −12.0‰;'}c) a wet paste pH of less than 12; and combinations thereof.3. The cementitious composition of claim 1 , wherein the composition comprising carbonate is a self-cement composition.4. The cementitious composition of claim 1 , wherein the composition comprising carbonate is a partial cement substitute.5. The cementitious composition of claim 1 , wherein the cementitious composition exhibits one or more of properties selected from the group consisting of higher reactivity of carbonate with aluminate phases claim 1 , formation of monocarboaluminates claim 1 , formation of hemicarboaluminates claim 1 , higher compressive strength claim 1 , higher durability over long time period claim 1 , higher mechanical and structural properties claim 1 , and combinations thereof claim 1 , as compared to CAC alone.6. The cementitious composition of claim 1 , wherein the composition comprising carbonate has a mean particle size of between 1-25 microns.7. The cementitious composition of claim 1 , wherein the cementitious composition further comprises ordinary Portland cement claim 1 , a Portland cement blend claim 1 , pozzolan-lime cement claim 1 , slag-lime cement claim 1 , supersulfated cement claim 1 , calcium sulfoaluminate cement claim 1 , geopolymer cement ...

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03-10-2013 дата публикации

METHODS AND SYSTEMS FOR UTILIZING CARBIDE LIME

Номер: US20130256939A1
Принадлежит: CALERA CORPORATION

Methods and systems are provided for producing a carbonate precipitation material comprising stable or reactive vaterite from carbide lime that provides both a source of divalent cations (Ca ions, Mg ions, etc.) and a source of proton removing agent. 1. A method comprising:a) contacting an aqueous solution comprising carbide lime with carbon dioxide from an industrial process; andb) producing a precipitation material comprising reactive vaterite.2. The method of claim 1 , further comprising purifying the carbide lime by treatment with weak base before step a) to make the aqueous solution comprising carbide lime.3. The method of claim 1 , further comprising purifying the carbide lime by treatment with weak base selected from borate claim 1 , N-containing salt claim 1 , N-containing aliphatic compound claim 1 , N-containing aromatic compound claim 1 , and combinations thereof claim 1 , before step a) to make an aqueous solution comprising carbide lime.4. The method of claim 3 , wherein the N-containing salt is selected from ammonium chloride claim 3 , ammonium sulfate claim 3 , ammonium nitrate claim 3 , and combinations thereof.5. The method of claim 2 , wherein molar ratio of the weak base:carbide lime is between 2:1 to 4:1.6. The method of claim 1 , further comprising subjecting the aqueous solution at step a) to one or more precipitation conditions that favor formation of the reactive vaterite.7. The method of claim 6 , wherein the one or more precipitation conditions are selected from temperature claim 6 , pH claim 6 , pressure claim 6 , ion ratio claim 6 , precipitation rate claim 6 , presence of additive claim 6 , presence of ionic species claim 6 , concentration of additive and ionic species claim 6 , stirring claim 6 , residence time claim 6 , mixing rate claim 6 , forms of agitation claim 6 , presence of seed crystal claim 6 , catalyst claim 6 , membrane claim 6 , or substrate claim 6 , dewatering claim 6 , drying claim 6 , ball milling claim 6 , and ...

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10-10-2013 дата публикации

INORGANIC MATERIAL BOARD

Номер: US20130263760A1
Принадлежит: NICHIHA CORPORATION

An inorganic material board, which is a cured mat formed by dehydrating a slurry including 30 to 53 wt % of blast furnace slag, 2 to 5 wt % of gypsum having an average particle size of 200 to 2000 μm, 5 to 11 wt % of alkaline material, 5 to 15 wt % of reinforcing fibers, and 31 to 50 wt % of inorganic admixture with respect to a total solid content, and in which a weight ratio of the blast furnace slag to the gypsum to the alkaline material is 1:0.05 to 0.15:0.15 to 0.35. It is desirable that the blast furnace slag has a specific surface area of 3000 to 5000. 1. An inorganic material board , which is a cured mat formed by dehydrating a slurry including 30 to 53 wt % of blast furnace slag , 2 to 5 wt % of gypsum having an average particle size of 200 to 2000 μm , 5 to 11 wt % of alkaline material , 5 to 15 wt % of reinforcing fibers , and 31 to 50 wt % of inorganic admixture with respect to a total solid content , and in which a weight ratio of the blast furnace slag to the gypsum to the alkaline material is 1:0.05 to 0.15:0.15 to 0.35.2. The inorganic material board according to claim 1 , wherein the blast furnace slag has a specific surface area of 3000 to 5000.3. The inorganic material board according to claim 1 , wherein a bending strength is not less than 10 N/m.4. The inorganic material board according to claim 1 , whereinthe blast furnace slag is granulated blast furnace slag;the gypsum is recycled gypsum obtained by crushing plasterboard waste;the inorganic material board containing any one or more of coal ash and papermaking sludge incineration ash as the inorganic admixture and containing wastepaper as the reinforcing fibers.5. The inorganic material board according to claim 4 , wherein claim 4 , a total of the granulated blast furnace slag claim 4 , the recycled gypsum claim 4 , the coal ash claim 4 , the papermaking sludge incineration ash and the wastepaper is 50 to 95 wt % with respect to total solid content.6. The inorganic material board according to ...

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24-10-2013 дата публикации

Plant for producing cement with central grinding unit

Номер: US20130277471A1
Автор: Strasser Siegfried
Принадлежит:

A plant for producing cement, having a first stage for crushing raw material to form raw powder, a second stage for calcination and sintering of the raw powder to form cement clinker, a third stage for cooling the sintered cement clinker, and a fourth stage for crushing the sintered cement clinker to form cement. The first stage for crushing raw material to form raw powder and the fourth stage for crushing the sintered cement clinker to form cement are structurally combined. In this way, during servicing or repair of one crushing stage, the plant need not be shut down because, y variable circuitry switching, the crushing stages permit plant operation with reduced production output. 15-. (canceled)6. A plant for producing cement , comprising:a first stage for crushing raw material to form raw powder,a second stage for calcining and sintering the raw powder to form cement clinker,a third stage for cooling the sintered cement clinker, anda fourth stage for crushing the sintered cement clinker to form cement,wherein the first stage for crushing raw material to form raw powder and the fourth stage for crushing the sintered cement clinker to form cement are combined structurally.7. The plant as claimed in claim 6 , wherein the first stage for crushing raw material to form raw powder and the fourth stage for crushing the sintered cement clinker to form cement are each constructed as a circulating grinding system with separators claim 6 , wherein at least one gas feed line leads from the remaining stages of the plant into the first stage and into the fourth stage claim 6 , and conduct gas for separating the circulating grinding systems of the first stage and fourth stage.8. The plant as claimed in claim 7 , wherein the separators are separated structurally from the first stage for crushing raw material to form raw powder and from the fourth stage for crushing the sintered cement clinker to form cement.9. The plant as claimed in claim 8 , wherein the separator for the first ...

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31-10-2013 дата публикации

DIMENSIONALLY STABLE GEOPOLYMER COMPOSITIONS AND METHOD

Номер: US20130284069A1
Автор: DUBEY Ashish
Принадлежит:

A method for making geopolymer cementitious binder compositions for cementitious products such as concrete, precast construction elements and panels, mortar and repair materials, and the like is disclosed. The geopolymer cementitious compositions of some embodiments are made by mixing a synergistic mixture of thermally activated aluminosilicate mineral, calcium aluminate cement, a calcium sulfate and a chemical activator with water 1. An aluminosilicate geopolymer composition comprising the reaction product of a thermally activated aluminosilicate mineral; a calcium aluminate cement; a calcium sulfate selected from the group consisting of calcium sulfate dihydrate , calcium sulfate hemihydrate , anhydrous calcium sulfate and mixtures thereof; a chemical activator selected from the group consisting of an alkali metal salt and an alkali metal base and mixtures thereof , and water.2. The aluminosilicate geopolymer composition of comprising the reaction product of about 35 to about 96% by weight of the thermally activated aluminosilicate mineral claim 1 , about 2 to about 45% by weight of the calcium aluminate cement claim 1 , about 1 to about 45% by weight of the calcium sulfate claim 1 , about 1.0 to about 6.0% by weight of the chemical activator selected from the group consisting of an alkali metal salt and an alkali metal base claim 1 , and water.3. The composition of claim 1 , wherein the chemical activator comprises an alkali metal citrate and the thermally activated aluminosilicate mineral comprises Class C fly ash.4. The composition of claim 1 , comprising a reaction product of amounts of the chemical activator and calcium sulfate relative to the amounts of the thermally activated aluminosilicate mineral and calcium aluminate cement effective to cause the reaction product to set in a predetermined time after mixing with water.5. The composition of claim 4 , wherein the amounts of the chemical activator and calcium sulfate relative to the amounts of thermally ...

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31-10-2013 дата публикации

COMPOSITION FOR BUILDING MATERIALS HAVING IMPROVED FREEZE-THAW RESISTANCE AND PROCESS FOR THE PRODUCTION THEREOF

Номер: US20130284071A1
Принадлежит: EVONIK DEGUSSA GmbH

A hydraulically curable composition, in particular for the production of concrete, mortar, screed, or render having improved freeze-thaw resistance, as well as a process for producing the composition. The composition includes the constituents cement, additional constituents, and organofunctional silicon compounds, and optionally aggregates and admixtures. The composition also contains the additional constituents fly ash and silica dust, in each case independently based on the weight of cement, in an amount of from 1 to 25% by weight and the organofunctional silicon compounds in an amount of from 0.1 to 5% by weight based on the weight of cement. 1. A hydraulically curable composition comprising:cement;additional constituents;organofunctional silicon compounds;fly ash;silica dust;optionally aggregates; andoptionally admixtures;wherein the fly ash is present in an amount of from 1 to 25% by weight based on the weight of cement;wherein the silica dust is present in an amount of from 1 to 25% by weight based on the weight of cement; andwherein the organofunctional silicon compounds are present in an amount of from 0.1 to 5% by weight based on the weight of cement.2. The composition according to ;wherein the fly ash is present in an amount of from 5 to 20% by weight based on the weight of cement; andwherein the silica dust is present in an amount of from 5 to 20% by weight based on the weight of cement.3. The composition according to ;characterized in thatwherein the fly ash is present in an amount of from 5 to 15% by weight based on the weight of cement;wherein the silica dust is present in an amount of from 5 to 15% by weight based on the weight of cement; andwherein the organofunctional silicon compounds are present in an amount of from 0.1 to 5% by weigh based on the weight of cement.4. The composition according to ;wherein the fly ash and the silica dust are present in a ratio of from 1:10 to 10:1.5. The composition according to ;wherein the organofunctional silicon ...

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07-11-2013 дата публикации

DRY GROUT COMPOSITION AND CAPSULE FOR ANCHORING REINFORCING MEMBER, DOWEL OR ANCHOR ELEMENTS

Номер: US20130294845A1
Автор: BERTRAND JACQUES
Принадлежит:

A dry grout composition including a calcium aluminosulfate based hydraulic cement, a mineral filler, a thixotropic agent, and a superplasticizer agent. Also, an anchoring capsule, containing the dry grout composition, for use in anchoring reinforcing member dowel, or anchor elements in a hole of a substrate, and a method of use. 1. A cementitious anchoring capsule for use in anchoring a reinforcing member , dowel or anchor elements in a hole of a substrate , the capsule comprising:a water permeable encapsulating means wherein the encapsulating means is made of polyester; and 40% to 70% of a calcium aluminosulfate based hydraulic cement;', '40% to about 60% mineral filler which is sand;', '0.01% to about 5% of a thixotropic agent which is a cellulose-based colloidal agent; and', '0.01% to about 5% of a melamine sulfonate based superplasticizer agent,, 'a grout composition comprisingsaid amounts being based upon the total dry weight of said composition for a total of 100%, andsaid grout composition being encapsulated within said encapsulating means.2. The anchoring capsule as defined in claim 1 , wherein the cement contains less than 30% of alumina.3. The anchoring capsule as defined in claim 1 , wherein the cement contains between about 10% and about 25% of alumina.4. The anchoring capsule as defined in claim 1 , wherein the cement contains less than about 15% of alumina.5. The anchoring capsule as defined in claim 1 , wherein the grout composition contains about 1% thixotropic agent.6. The anchoring capsule as defined in claim 1 , wherein the grout composition contains less than about 0.1% thixotropic agent.7. The anchoring capsule as defined in claim 1 , wherein the grout composition contains from about 45% to about 55% mineral filler.8. The anchoring capsule as defined in claim 1 , wherein the grout composition further comprises class F flyash and/or silica fume compliant with ASTM C 1240.9. The anchoring capsule as defined in claim 1 , wherein the grout ...

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14-11-2013 дата публикации

HYDRAULIC BINDER WITH LOW CLINKER CONTENT

Номер: US20130298805A1
Принадлежит: LAFARGE

A hydraulic binder includes, in parts by mass: (a) from 20 to 60 parts of Portland clinker; (b) from 20 to 40 parts of slag; and (c) from 0 to 60 parts of inorganic material other than the clinker and the slag; the sum of (a), (b) and (c) being equal to 100 parts; which binder further includes a slag activator including, relative to 100 parts of the sum of (a) and (b): from 1.4 to 6.55 parts of alkali metal salt, expressed as equivalent—NaO; and from 1.1 to 11.0 parts of calcium sulfate, expressed as SO. 1. Hydraulic binder comprising , in parts by mass:(a) from 20 to 60 parts of Portland clinker;(b) from 20 to 40 parts of slag; and(c) from 0 to 60 parts of inorganic material other than the clinker and the slag;the sum of (a), (b) and (c) being equal to 100 parts;which binder further comprises a slag activator comprising, relative to 100 parts of the sum of (a) and (b):{'sub': '2', 'from 1.4 to 6.55 parts of alkali metal salt, expressed as equivalent—NaO; and'}{'sub': '3', 'from 1.1 to 11.0 parts of calcium sulfate, expressed as SO.'}2. A hydraulic binder according to claim 1 , wherein the Blaine specific surface of the Portland clinker is greater than or equal to 5500 cm/g.3. A hydraulic binder according to or wherein the alkali metal salt is sodium sulfate.4. A hydraulic binder according to any one of to claim 1 , wherein the inorganic material comprises a pozzolan claim 1 , fly ash claim 1 , calcined shale claim 1 , calcium carbonate claim 1 , silica fume claim 1 , metakaolin or a mixture thereof.5. A hydraulic binder according to any one of to claim 1 , wherein the inorganic material comprises an inert filler.6. A hydraulic binder according to any one of to claim 1 , comprising no alkali metal hydroxide.7. A hydraulic binder according to any one of to claim 1 , comprising no fly ash.87. A hydraulic composition comprising a hydraulic binder according to any one of to claims 1 , aggregate and water.9. A process for preparing a hydraulic composition according to ...

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21-11-2013 дата публикации

COATING COMPOSITIONS FOR ROOFING GRANULES, DARK COLORED ROOFING GRANULES WITH INCREASED SOLAR HEAT REFLECTANCE, SOLAR HEAT-REFLECTIVE SHINGLES, AND PROCESS FOR PRODUCING THE SAME

Номер: US20130305961A1
Принадлежит:

Dark colored roofing granules include an inert base particle coated with a composition including a metal silicate, a non-clay latent heat reactant, and a dark colored but solar reflective pigment.

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28-11-2013 дата публикации

METHOD AND INSTALLATION FOR PRODUCING CLINKER

Номер: US20130312640A1
Автор: Zurhove Franz-Josef
Принадлежит: ELEX CEMCAT AG

The invention relates to a process and a plant for producing cement clinker, which has a furnace system and has essentially the following process steps:—raw material is preheated in a preheater by means of hot offgases from the furnace system,—dust is removed from the hot offgas downstream of the preheater in a preliminary dust removal apparatus to a residual dust concentration of max. 20 g/standard m,—the offgas which has been subjected to preliminary dust removal is purified in a selective catalytic flue gas purification plant (selective catalytic reduction, SCR),—at least part of the offgas purified in the flue gas purification plant is conveyed in a bypass around a raw material milling plant to a cooling device and cooled there to temperatures of max. 140° C.,—before the residual dust in the offgas is precipitated in a process filter and—at least part of the residual dust precipitated in the process filter is discharged for removal of mercury. 2. Method according to claim 1 , characterised in that claim 1 , for improved mercury adsorption downstream of the cooling device claim 1 , there is injected into the exhaust gas an additional adsorbent which is separated in the process filter together with the residual dust.3. Method according to claim 1 , characterised in that the exhaust gas in the cooling device is reduced to a maximum of 125° C. claim 1 , preferably to a maximum of 110° C.4. Method according to claim 1 , characterised in that the hot exhaust gas downstream of the preheater in the preliminary dust removal device is dedusted to a residual dust concentration of a maximum of 10 g/Nm claim 1 , preferably to a maximum of 5 g/Nm.5. Method according to claim 1 , characterised in that a portion of the residual dust separated in the process filter is recirculated and another portion is flushed out for mercury cleaning.6. Method according to claim 5 , characterised in that at least a portion of the residual dust cleaned in respect of the mercury is recirculated ...

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05-12-2013 дата публикации

Use Of Compounds Containing Aluminium Oxide And Silicon Oxide For Producing A Hydrophilic Building Product

Номер: US20130319294A1
Принадлежит: Construction Research & Technology GmbH

The use of a binder system comprising compounds containing aluminium oxide and silicon oxide for producing a hydrophilic building product, characterized in that the sum of the oxides calculated as AlOand SiOin the binder system is ≧40% by weight, based on the water-free binder system, and the contact angle of an oil drop placed on the surface of the cured building product is ≧90°, where the contact angle determination is carried out under water, is proposed. The said hydrophilicity makes the building product easy to clean, with simple rinsing with water often being sufficient. 117-. (canceled)18. A hydrophilic building product obtained by contacting with water , setting and curing a binder system comprising compounds containing aluminium oxide and silicon oxide , wherein the sum of the oxides calculated as AlOand SiOin the binder system is ≧40% by weight , based on a water-free binder system , and the contact angle of an oil drop placed on the surface of the cured building product is ≧90° , where the contact angle determination is carried out under water.19. The building product according to claim 18 , wherein the sum of the oxides calculated as AlOand SiOin the binder system is ≧50% by weight based on the water-free binder system.20. The building product according to claim 18 , wherein the contact angle is ≧100°.21. The building product according to claim 18 , wherein the content of the oxides calculated as SiOin the binder system is ≧15% by weight claim 18 , based on the water-free binder system.22. The building product according to claim 18 , wherein the binder system further comprises compounds containing titanium oxide and/or zirconium oxide and the sum of the oxides calculated as AlO claim 18 , SiO claim 18 , TiOand ZrOin the binder system is ≧41% by weight claim 18 , based on the water-free binder system.23. The building product according to claim 18 , wherein the content of oxides calculated as CaO in the binder system is ≦35% by weight claim 18 , based on ...

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26-12-2013 дата публикации

PROCESS AND PLANT FOR CEMENT CLINKER PRODUCTION

Номер: US20130340650A1
Принадлежит:

Plant and process for cement clinker production includes preheating a raw meal, a calcination step where the raw meal is brought to a temperature of about 800-850° C. to substantially decompose its mineral constituents into their oxides, and a sintering step where the load is brought to a temperature of 1300 to 1450° C. to form CaSiO(or (CaO).SiO), to further decompose calcium carbonate and partially melt the load to form Ca.SiO(or (CaO).SiO) in a rotarykiln, followed by cooling the resulting clinker, and optionally milling it, wherein untreated oil sludge is supplied into an injection zone of the calcination zone operated at a material temperature of approx. 800-850° C., the injection zone including the bottom discharge of the lowest cyclone stages and/or of the precalciner, if appropriate, the feed-in slope of the rotary kiln and the gas phase over the mineral bed at the material inlet end of the rotary kiln. 115-. (canceled)16. A process for cement production including a raw meal preheating step performed in a preheating zone , a calcination step in which the raw meal is brought to a temperature of approximately 800-850° C. leading to substantial decomposition of the mineral constituents of the raw meal into their oxides , and a sintering step in which the load is brought to a temperature of 1300 to 1450° C. to form CaSiO(or (CaO).SiO) , to further decompose calcium carbonate and partially melt the load to form Ca.SiO(or (CaO).SiO) in a rotary kiln , followed by cooling of the resulting clinker in a clinker cooling zone , and optionally by a clinker milling step in a clinker milling zone , wherein oil sludge is supplied in an injection zone comprised within the calcination zone , operated at a material temperature of approx. 800-850° C. , said injection zone comprising the bottom discharge of the lowest cyclone stages and/or of the precalciner , if appropriate , the feed-in slope of the rotary kiln and the gas phase over the mineral bed at the material inlet end ...

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13-02-2014 дата публикации

CO2-SEQUESTERING FORMED BUILDING MATERIALS

Номер: US20140041553A1
Принадлежит: CALERA CORPORATION

CO-sequestering formed building materials are provided. The building materials of the invention include a composition comprising a carbonate/bicarbonate component. Additional aspects of the invention include methods of making and using the CO-sequestering formed building material. 130-. (canceled)31. A formed building material , comprising: a sequestered-COcomponent , wherein the sequestered-COcomponent comprises at least 50% w/w calcium carbonate wherein the calcium carbonate comprises vaterite , aragonite , or combinations thereof , wherein the sequestered-COcomponent has a δC less than −15% , and wherein the formed building material is a construction panel.32. The formed building material of claim 31 , wherein the construction panel is a cement board.33. The formed building material of claim 32 , wherein the cement board has a flexural strength of between 1-7.5 MPa claim 32 , compressive strength of between 5-50 MPa claim 32 , or both.34. The formed building material of claim 32 , wherein the cement board further comprises fiberglass.35. The formed building material of claim 31 , wherein the construction panel is a drywall.36. The formed building material of claim 35 , wherein the drywall has a flexural strength of between 0.1-3 MPa claim 35 , compressive strength of between 1-40 MPa claim 35 , or both.37. The formed building material of claim 35 , wherein the drywall further comprises paper claim 35 , gypsum claim 35 , fiberglass claim 35 , or combinations thereof.38. The formed building material of claim 31 , wherein the construction panel is a fiber-cement siding.39. The formed building material of claim 38 , wherein the fiber-cement siding has a flexural strength of between 0.5-5 MPa claim 38 , compressive strength of between 2-25 MPa claim 38 , or both.40. The formed building material of claim 31 , wherein the formed building material has a compressive strength of between 5-100 MPa.41. The formed building material of claim 31 , wherein the construction panel ...

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20-02-2014 дата публикации

CEMENTITIOUS BINDERS AND WOOD PARTICLES-BASED INCOMBUSTIBLE COLOURED COMPOSITE PANEL WITH STRUCTURAL HIGH PERFORMANCE

Номер: US20140047997A1

A composite panel is made from wood and cementitious binders, with flat surfaces and several possible colours. The panel comprises 35 to 85% of grey or white Portland cement; 10 to 30% of debarked resinous wood particles; 5 to 20% of semi-hydrated calcium sulphate; 0 to 10% of a surface accelerator; 0 to 10% of aluminium sulphate solution; 0 to 30% of calcium carbonate; and 0 to 15% of pigments. The process of preparation for the existing VIROC panel is adjusted to the new material. This panel, in addition to being very resistant and showing high performances in terms of resistance to impact, humidity, temperature variation, noise and fungi, as well as other microorganisms, also complies with all the requirements of the associated product standard. 1. An incombustible composite panel of high performance , made from Portland cement , gypsum and wood particles , comprising in weight percentage of the components with reference to the dry weight of the composition:1) 35 to 85% of grey or white Portland cement;2) 10 to 30% of debarked resinous wood particles;3) 5 to 20% of semi-hydrated calcium sulphate;4) 0 to 10% of a surface accelerator;5) 0 to 10% of aluminium sulphate solution;6) 0 to 30% of calcium carbonate; and7) 0 to 15% of pigments.2. The composite panel according to claim 1 , wherein the resinous wood used in order to obtain the component 2) is pinewood.3. The composite panel according to claim 1 , wherein that the wood particles used as the component 2) are in the form of chips.4. The composite panel according to claim 3 , wherein the thickness of the said chips ranges from 0.25 to 0.32 mm.5. The composite panel according to claim 3 , wherein 50 to 70% of the said chips are <1 mm long claim 3 , and 26 to 40% of the said chips have a length of 1 to 4 mm.6. The composite panel according to claim 1 , wherein the surface accelerator used as the component 4) is sodium silicate solution with a density ranging from 1.10 to 1.15 g/cm.7. The composite panel according ...

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20-02-2014 дата публикации

ACID AND HIGH TEMPERATURE RESISTANT CEMENT COMPOSITES

Номер: US20140047999A1
Автор: Ràzl Ivan
Принадлежит:

Process for production of acid and high temperature resistant cement composites, where the matrix is alkali activated F fly ash alone, F Fly ash combined with ground slag or ground slag alone. F-fly ash produces lower quality alkali activated cement systems. On the other hand the lack of calcium oxide results in very high resistance to medium and highly concentrated inorganic or organic acids. The high strength and low permeability of pure F-fly ash cement systems is achieved by using in the composition un-densified silica fume, the amorphous silicone dioxide obtained as by products in production of ferro-silicones. Precipitated nano-particle silica made from soluble silicates and nano-particle silica fume produced by burning silicon tetra chloride in the hydrogen stream. 1. Acid and high temperature resistant cement composites , comprising a matrix of F fly ash particles ranging from 1 micron to 150 microns and/or ground slag containing around 30% by weight of calcium oxide alkali activated by sodium silicate and/or potassium hydroxides in combination with alkali metal silicates , where a concentration of potassium or sodium hydroxides varies from 3.0% to 15.0% by weight , based on a weight of the matrix (binder) , defined as a weight of F-Fly ash alone or F-Fly ash in combination with ground slag , a concentration of liquid sodium or potassium silicate varies from 3-30% by weight , based on liquid sodium or potassium silicates , containing 8.9% NaO or KO and 28.7% SiO , this based on a weight of the matrix (binder) , when using solid sodium or potassium silicates , a typical content varies from 1% to 15% by a weight of the matrix (binder) , this based on the weight of the matrix (binder) , wherein solid sodium or potassium silicates contain 19% NaO or KO and 61% of SiO2. Acid and high temperature resistant cement composites according to claim 1 , comprising retarders comprising at least one of citric acid claim 1 , sodium citrate claim 1 , tartaric acid and sodium ...

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06-03-2014 дата публикации

Cement clinker manufacturing plant

Номер: US20140065028A1
Принадлежит: Vicat SA

A cement clinker manufacturing plant that includes a plant for producing purified syngas, obtained from solid waste, and process for transferring ash recovered from the ash pan of the gasifier to at least one inlet of the feedstock conversion device, which the plant includes, and/or of the furnace for the purpose of incorporating said ash into the feedstock; and a process for conveying the purified syngas to the main tuyere of the furnace and/or to at least one inlet of the feedstock conversion device.

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01-01-2015 дата публикации

OPTIMIZATION OF THE PROPERTIES OF ALUMINOUS CEMENTS USING INORGANIC FILLERS

Номер: US20150000568A1
Принадлежит:

The carefully controlled addition of inorganic fillers to calcium sulfoaluminate rapid-setting cements can lead to significant improvement and optimization of its properties. Generally, prior art achieves cement optimization using costly and unstable organic additives. In the present invention, the addition of three inorganic additives such as coal ash, limestone or kiln dust led to appreciable improvement in the properties of calcium sulfoaluminate-containing cements. The addition of coal fly ash led to increased compressive strength and freeze-thaw durability while decreasing shrinkage and autoclave expansion. The addition of limestone was shown to control the compressive strength while not affecting the setting time, and the addition of cement kiln dust was shown to control the compressive strength while increasing the setting time. And finally, the presence of a super plasticizing agent was shown to negatively affect both compressive strength and shrinkage when used in combination with fly ash. 1. A rapid-setting material consisting of calcium sulfoaluminate cement and coal fly ash , the amount of coal fly ash being up to 30% by weight of the material.2. The material of wherein the coal fly ash content is at least approximately 5% by weight.3. The material of wherein the amount of coal fly ash is 10-30 wt % coal fly ash claim 1 , whereby the resulting 1.5 hour claim 1 , 3 hour or 24 hour compressive strength is increased by 500 to 1 claim 1 ,000 psi compared to the strength of the pure calcium sulfoaluminate-containing cement.4. The material of which passes autoclave testing due to the addition of coal fly ash.5. The material of in which ettringite content has increased after hydration claim 1 , when compared to calcium sulfoaluminate cement without coal fly ash.6. The cement of which claim 1 , when tested using ASTM C 157 claim 1 , exhibits a shrinkage of less than 0.02% at 28 days.7. A rapid-setting material comprising calcium sulfoaluminate cement and coal ...

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06-01-2022 дата публикации

Additive For Blended Cement Compositions, Cement Produced Therefrom And Methods Related Thereto

Номер: US20220002197A1
Принадлежит: Carbon Capture Machine (Uk) Limited

The present invention relates to a cement additive for use in a blended cement composition, the additive comprising a precipitated calcium carbonate formed from mineral sequestration of carbon dioxide.

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07-01-2021 дата публикации

HYALOCLASTITE, SIDEROMELANE OR TACHYLITE POZZOLAN-BASED GEOPOLYMER CEMENT AND CONCRETE AND METHOD OF MAKING AND USING SAME

Номер: US20210002171A1
Принадлежит:

The invention comprises a cementitious material comprising a natural pozzolan selected from hyaloclastite, sideromelane or tachylite, wherein the natural pozzolan has a volume-based mean particle size of less than or equal to 40 μm. The cementitious material also comprising an aqueous alkaline activating solution suitable for forming a geopolymer. A method making a cementitious material is also disclosed. 1. A cementitious material comprising:a natural pozzolan selected from hyaloclastite, sideromelane, tachylite or combinations or mixtures thereof, wherein the natural pozzolan has a volume-based mean particle size of less than or equal to approximately 40 μm; andan aqueous alkaline activating solution suitable for forming a geopolymer.2. The cementitious material of claim 1 , wherein the natural pozzolan has a volume-based mean particle size of less than or equal to approximately 20 μm.3. The cementitious material of claim 1 , wherein the natural pozzolan has a volume-based mean particle size of less than or equal to approximately 10 μm.4. The cementitious material of claim 1 , wherein the natural pozzolan has a volume-based mean particle size of less than or equal to approximately 5 μm.5. The cementitious material of claim 1 , wherein the aqueous alkaline activating solution comprises a hydroxide selected from NaOH claim 1 , KOH claim 1 , CaOH claim 1 , and other minerals or compounds having reactive hydroxyl groups.6. The cementitious material of claim 5 , wherein the hydroxide is sodium hydroxide or potassium hydroxide.7. The cementitious material of claim 5 , wherein the aqueous alkaline activating solution further comprises a water-soluble alkali metal silicate.8. The cementitious material of claim 7 , wherein the water-soluble alkali metal silicate is sodium silicate or potassium silicate.9. The cementitious material of claim 1 , wherein the aqueous alkaline activating solution comprises sodium hydroxide or potassium hydroxide and sodium silicate or potassium ...

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04-01-2018 дата публикации

Dry grout composition and capsule for anchoring reinforcing member, dowel or anchor elements

Номер: US20180002228A1
Автор: Jacques Bertrand
Принадлежит: Individual

A dry grout composition including a calcium aluminosulfate based hydraulic cement, a mineral filler, a thixotropic agent, and a superplasticizer agent. Also, an anchoring capsule, containing the dry grout composition, for use in anchoring reinforcing member dowel, or anchor elements in a hole of a substrate, and a method of use.

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04-01-2018 дата публикации

A HYDRAULIC COMPOSITION FOR THE CONSTRUCTION OF PAVEMENTS

Номер: US20180002232A1
Принадлежит:

A hydraulic composition for the construction of pavements, and in particular for the repair of pavements, includes a hydraulic binder including a cement, 0.18% to 0.35% of a superplasticiser, where the percentage is expressed by dry weight compared to the cement, and where the superplasticiser includes a branched polymer including at least one pendant chain, with a terminal function of the phosphonate or phosphate type, and 0.25% to 2% of a setting accelerator, where the percentage is expressed by dry weight compared to the cement, where the setting accelerator includes a calcium salt, where the hydraulic composition has a Water/Cement ratio higher than 0.38 and strictly less than 0.45. 19-. (canceled)10- A hydraulic composition for the construction of pavements comprising:a hydraulic binder comprising a cement,0.18% to 0.35% of a superplasticiser, the percentage being expressed by dry weight compared to the cement, and said superplasticiser comprising a branched polymer including at least one pendant chain, with a terminal function of the phosphonate or phosphate type, and0.25% to 2% of a setting accelerator, the percentage being expressed by dryweight compared to the cement, said setting accelerator comprising a calcium salt, said hydraulic composition having a Water/Cement ratio higher than 0.38 and strictly less than 0.45.11- The hydraulic composition according to claim 10 , wherein the number of pendant chains is less than or equal to three.12- The hydraulic composition according to claim 10 , wherein the calcium salt comprises a calcium nitrite claim 10 , a calcium nitrate or their blends.13- The hydraulic composition according to claim 10 , wherein the cement comprises a Portland cement of the CEM I type according to Cement standard NF EN 197-1.14- The hydraulic composition according to claim 13 , wherein the Portland cement of CEM I type is in resistance category 42.5 N claim 13 , 42.5 R claim 13 , 52.5 N or 52.5 R according to Cement standard NF EN 197-1.15 ...

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02-01-2020 дата публикации

SYSTEM AND METHOD FOR IMPROVED PORTLAND CEMENT BASECOAT PLASTERS

Номер: US20200002230A1
Принадлежит:

Systems and methods according to present principles enhance aspects of applied plaster coats. In particular, the materials include a synthetic substitute aggregate (SSA), added to a cementitious base coat, for a plastering step prior to application of stucco or acrylic synthetic finishes or finish coats. The addition of SSA to a pre-blended cementitious base coat creates a light weight product which in some implementations is highly advantageous for the plastering industry. 1. A method of using a lightweight plaster , the method comprising:a. performing a first step of making a lightweight plaster by mixing together in a mixer a first aggregate constituting between about 40 and 70% by weight of the plaster product and a binder constituting between about 20 and 40% by weight of the plaster product, and adding to the mixer a synthetic substitute aggregate occupying a same volume as the first aggregate plus or minus 10%;b. performing a second step of making a lightweight plaster by mixing together in a mixer a product of step (a) with water;c. applying the lightweight plaster as a coating to a vertical wall including a lath, lattice, or other substrate, to a thickness of about ⅜″ to ⅞″, such that the lightweight plaster acts as a base coat to plumb the vertical wall and to create a base to receive a finish coat application, the finish coat application being a stucco or acrylic synthetic finish or finish coat, such that only one lightweight plaster coating is required rather than two or more; andd. applying the finish coat application onto the lightweight plaster coating,e. such that a lightweight plaster coating is made and used to allow an end user to apply a plaster coating that is less in weight than prior plaster coatings while realizing no loss of yield per bag, and in which a lightweight plaster coating is achieved that provides greater insulative properties as compared to traditional base coats.2. The lightweight plaster of claim 1 , wherein the synthetic ...

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07-01-2021 дата публикации

Cooler

Номер: US20210003346A1
Автор: Føns Mogens Juhl
Принадлежит:

The present invention relates to a cooler for cooling particulate material which has been subjected to heat treatment in an industrial kiln, such as a rotary kiln for manufacturing cement clinker. This cooler comprises an inlet, an outlet, end wall, side walls, a bottom and a ceiling, at least three reciprocating supporting lanes for receiving, supporting and transporting the material to be cooled, the lanes are moving following the walking floor principles as well as means for injecting cooling gas into the material through grate plates in the lanes. The present invention relates to an increasing in the vertical shearing height, and still having stationary clinker on top of the grate plates, see FIG. . The length of the tilted element () is L and the distance () between two devices is G. The angle between the element () and horizontal is alfa (). Since the air is distributed evenly from the full grate plate area it is obvious and understandable that the L*cosines(alfa) becomes a shadow area where all air from the region in the grate plate will go through the stationary clinker and leave the tip of L at this one point only. Again, it is not good for the heat recuperation to have a shadow area too big—as it, again, gives an uneven air flow through the clinker bed, damaging the heat recuperation. The vertical shearing height is on the other hand L*sinus(alfa). But if alfa becomes too large (approximately above 60 deg.), it will block the sliding effect, as now the clinker will not get forced over the plate's L-part, and then the wished larger vertical shearing is not achieved. It is hereby a compromise to get a certain vertical shearing: L*sinus(alfa) by not having a too large shadow area L*cosines(alfa), but still having the angle alfa so low that the clinker will slide at L—see FIG.

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01-01-2015 дата публикации

HYDRAULIC COMPOSITION

Номер: US20150005414A1
Принадлежит:

A method includes providing a hydraulic composition, wherein a setting time of the hydraulic composition is greater than or equal to 12 hours without triggering the setting of the hydraulic composition and a variation of the slump of the hydraulic composition measured according to the EN 12350-2 Standard, is less than 50 mm or a variation of the spread of the hydraulic composition measured with a cone according to the EN 12350-2 Standard, is less than 100 mm for at least 12 hours without triggering the setting of the hydraulic composition; and storing the hydraulic composition in a closed container; wherein storing of the hydraulic composition occurs for at least 12 hours without mixing, after which the hydraulic composition is useable without further mixing. 1. A method comprising: (1) from 220 to 500 kg, per cubic metre of hydraulic composition, of a hydraulic binder comprising Portland cement;', '(2) from 400 to 1800 kg, per cubic metre of fresh hydraulic composition, of a sand having a D10 greater than 0.1 mm and a D90 less than 4 mm;', '(3) from 0.1 to 5% by mass of dry extract relative to the mass of hydraulic binder, of a retarding agent comprising a carboxylic acid, a phosphonic acid or salts thereof;', '(4) from 0.05 to 5% by mass of dry extract relative to the mass of hydraulic binder, of a superplasticizer comprising a polyphosphate polyoxyalkylene polymer, a polyphosphonate polyoxyalkylene polymer, a. polysulfonate polyoxyalkylene polymer or a polycarboxylate polyoxyalkylene polymer, and', '(5) from 0.01 to 2% by mass of dry extract relative to the mass of hydraulic binder, of a rheology-modifying agent comprising a cellulose or a derivative of cellulose,', 'wherein a setting time of the hydraulic composition is greater than or equal to 12 hours without triggering the setting of the hydraulic composition and a variation of the slump of the hydraulic composition measured according to the EN 12350-2 Standard, is less than 50 mm or a variation of the spread ...

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08-01-2015 дата публикации

LOW-ALKALI FLY ASH CEMENT AND METHOD OF MAKING

Номер: US20150007751A1
Принадлежит:

A method for making a low-alkali fly ash cement includes forming a mixture of class C fly ash and an aqueous solution and forming low-alkali fly ash cement from the mixture. The aqueous solution has an alkali at a molar concentration between about 0.002 M and about 2 M. A low-alkali fly ash cement includes class C fly ash and an alkali activating agent. The low-alkali fly ash cement contains between about 3×10wt % alkali activating agent and about 2 wt % alkali activating agent. A method for making fly ash cement includes forming a mixture of class C fly ash and water, wet pressing the mixture and forming fly ash cement from the mixture by curing the mixture at a temperature between about 60° C. and about 90° C. 1. A method for making a low-alkali fly ash cement , the method comprising:forming a mixture of class C fly ash and an aqueous solution, wherein the aqueous solution comprises an alkali at a molar concentration between about 0.002 M and about 2 M; andforming low-alkali fly ash cement from the mixture.2. The method of claim 1 , wherein the alkali is selected from the group consisting of hydroxides claim 1 , carbonates claim 1 , bicarbonates claim 1 , silicates claim 1 , chlorides claim 1 , sulfates and combinations thereof.3. The method of claim 2 , wherein the alkali is selected from the group consisting of NaOH claim 2 , KOH claim 2 , Ca(OH) claim 2 , Mg(OH) claim 2 , NaCO claim 2 , NaHCO claim 2 , NaSiO claim 2 , NaCl claim 2 , CaCl claim 2 , MgCl claim 2 , NaSOand combinations thereof.4. The method of claim 3 , wherein the alkali is sodium hydroxide.5. The method of claim 3 , wherein the alkali is sodium carbonate.6. The method of claim 3 , wherein the alkali is calcium hydroxide.7. The method of claim 6 , wherein the aqueous solution comprises a waste material selected from the group consisting of lime kiln dust claim 6 , cement kiln dust claim 6 , red mud and combinations thereof.8. The method of claim 3 , wherein the mixture further comprises insoluble ...

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10-01-2019 дата публикации

3D PRINTING OF BUILDING ELEMENTS AND BUILDINGS WITH BCT CEMENT

Номер: US20190009428A1
Принадлежит: HEIDELBERGCEMENT AG

The present invention relates to the use of belite calcium sulfoaluminate ternesite cement for the production of components and buildings by means of 3D printing and a method for the production of components and buildings by the 3D printing of belite calcium sulfoaluminate ternesite cement. 1. A use of belite calcium sulfoaluminate ternesite cement as a building material for the production of building elements and buildings by means of 3D printing.2. Use according to claim 1 , wherein the belite calcium sulfoaluminate ternesite cement contains{'sub': 5', '2, '5 to 75% by weight CS$'}{'sub': 4', '3, '5 to 70% by weight CA$'}{'sub': '2', '1 to 80% by weight CS and'}0 to 30% by weight secondary phaseswherein the total of all phases contained is 100% by weight.3. The use according to claim 1 , wherein the secondary phases in belite calcium sulfoaluminate ternesite cement are one or more of calcium silicates claim 1 , sulphates claim 1 , calcium aluminates claim 1 , spinels claim 1 , representatives of melilite group claim 1 , periclase claim 1 , free lime claim 1 , quartz and/or a glass phase.4. The use according to claim 1 , wherein the secondary phases are present in a proportion of 0.1% by weight to 30% and particularly preferred from 10% by weight to 15% by weight.5. The use according to claim 1 , wherein the belite calcium sulfoaluminate ternesite cement contains 10-60% by weight claim 1 , in particular{'sub': 5', '2, '20-40% by weight CS$, 10-60% by weight, in particular'}{'sub': 4', '3', '2, '20-45% by weight CA$ and 10-65% by weight, in particular 20-50% by weight CS.'}6. The use according to claim 1 , wherein at the free lime content in the belite calcium sulfoaluminate ternesite cement is below 5% by weight claim 1 , in particular below 2% by weight and most preferably below 1% by weight.7. The use according to claim 1 , wherein there is an X-ray amorphous phase or glass phase in an amount of 1 to 10% by weight claim 1 , preferably 2 to 8% by weight and in ...

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11-01-2018 дата публикации

PROCESS FOR THE PREPARATION OF HIGH ALUMINA CEMENT

Номер: US20180009710A1
Принадлежит:

High alumina cement is produced in a submerged combustion melter, cooled and ground. 1. Process for the preparation of high alumina cement comprising:introducing a solid batch material for preparation of high alumina cement into a melter;melting the solid batch material in the melter by submerged combustion to form a liquid melt;withdrawing at least a portion of the liquid melt from the melter;cooling said discharged liquid melt to obtain solidified melt; andgrinding the solidified melt to appropriate grain size.2. The process of claim 1 , wherein the melting chamber walls are cooled claim 1 , for example comprising double steel walls separated by circulating cooling liquid claim 1 , preferably water claim 1 , and are not covered by a refractory lining.3. The process of claim 1 , wherein heat is recovered from the hot fumes and/or from the cooling liquid.4. The process of wherein heat is recovered from the hot fumes to preheat the raw materials.5. The process of wherein part at least of the melt is withdrawn continuously or batchwise from the melter.6. The process of wherein the submerged burners of the melter are controlled such that the melt volume is increased by at least 8% claim 1 , preferably at least 10% claim 1 , more preferably at least 15% or 20% claim 1 , compared to the volume the melt would have with no burners firing.7. The process wherein the submerged combustion is performed such that a substantially toroidal melt flow pattern is generated in the melt claim 1 , having a substantially vertical central axis of revolution claim 1 , comprising major centrally inwardly convergent flows at the melt surface; the melt moves downwardly at proximity of the vertical central axis of revolution and is recirculated in an ascending movement back to the melt surface claim 1 , thus defining an substantially toroidal flow pattern.8. The process of wherein the melting step comprises melting the solid batch material claim 1 , in a submerged combustion melter by ...

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11-01-2018 дата публикации

COMPOSITIONS OF LOW ACTIVATION CONCRETE AND USE THEREOF

Номер: US20180009711A1
Принадлежит:

The present invention relates to a low-activation concrete comprising high-purity limestone aggregate and white cement, or high-purity limestone aggregate and aluminous cement. The low-activation concrete reduces the content of Europium, Cobalt and Cesium, as well as the content of elements such as Aluminium, Sodium, and Magnesium, when compared to standard concrete compositions and compositions for low-activation concrete already known in the art. The use of the low-activation concrete for forming an interior wall of a particle accelerator vault is provided as well. 1. A low-activation concrete comprising high-purity limestone aggregate and white cement , or high-purity limestone aggregate and aluminous cement ,{'sub': '3', 'the high-purity limestone aggregate comprising more than 97.0% by weight CaCO,'}wherein in the low-activation concrete comprising high-purity limestone aggregate and white cement the Eu content is less than 0.04 ppm, the Co content is less than 0.80 ppm, and the Cs content is less than 0.1 ppm, andwherein in the low-activation concrete comprising high-purity limestone aggregate and aluminous cement the Eu content is less than 0.01 ppm, the Co content is less than 0.26 ppm, and the Cs content is less than 0.03 ppm.2. The low-activation concrete according to claim 1 , wherein the concrete comprises 75% to 95% by weight high-purity limestone aggregate.3. The low-activation concrete according to claim 1 , wherein the concrete comprises 75% to 85% by weight high-purity limestone aggregate.4. The low-activation concrete according to claim 1 , wherein the high-purity limestone aggregate comprises between 97.0% and 98.5% by weight CaCO.5. The low-activation concrete according to claim 1 , wherein the high-purity limestone aggregate comprises between 54.3% and 55.2% by weight CaO claim 1 , between 0.8% and 1.0% by weight MgO claim 1 , between 0.2% and 0.6% by weight SiO claim 1 , between 0.05% and 0.1% by weight FeO claim 1 , less than 0.3% by weight ...

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14-01-2021 дата публикации

ORGANIC SLUDGE TREATMENT DEVICE AND TREATMENT METHOD

Номер: US20210009455A1
Принадлежит:

To treat organic sludge while keeping facility costs, cement production efficiency, and a reduction in clinker production amount to a minimum. An organic sludge treatment device includes: a fractionation device that fractionates a preheated raw material R from a preheater cyclone C excluding a bottommost cyclone of a cement burning device a mixing device that mixes an organic sludge S with the fractionated preheated raw material, and that dries the organic sludge using sensible heat of the preheated raw material; and a supply device (mixture chute double-flap damper shut damper ) that supplies a mixture M from the mixing device to a calciner furnace of the cement burning device or to a duct disposed between a kiln inlet portion of a cement kiln and the calciner furnace. The treatment device may be provided with an introduction device for introducing an exhaust gas G including dust, odor and water vapor from the mixing device to a gas outlet of a bottommost cyclone A of the cement burning device. 2. The organic sludge treatment device as claimed in claim 1 , further comprising an introduction device for introducing an exhaust gas including dust claim 1 , odor and water vapor from the mixing device to a gas outlet of a bottommost cyclone of the cement burning device.3. The organic sludge treatment device as claimed in claim 2 , further comprising a cyclone dust collector to which the exhaust gas including dust claim 2 , odor and water vapor is introduced from the mixing device claim 2 , and which recovers coarse powder and returns the recovered coarse powder to the mixing device and discharges an exhaust gas including fine powder claim 2 , odor and water vapor to the introduction device.4. The organic sludge treatment device as claimed in claim 1 , further comprising a urea supply device for supplying particulate urea to the mixing device.5. The organic sludge treatment device as claimed in claim 1 , wherein temperature of a mixture from an outlet of the mixing device ...

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10-01-2019 дата публикации

Postponed Onset of Quicklime Hydration

Номер: US20190010087A1
Автор: Chun Byong-Wa
Принадлежит:

The present invention provides compositions and methods relative to controlling hydration onset of an alkaline earth metal oxide such as calcium oxide, comprising heating an inorganic alkaline earth metal oxide to sub-calcination temperatures in the presence of organic material comprising a carbohydrate, an amino-carboxylic acid, a hydroxycarboxylic acid, or a mixture thereof. Preferred treated particles comprise at least 40% and more preferably at least 80% by dry weight calcium oxide which is heated in the presence of ascorbic acid and a starch. Treated particles of the present invention manifest an unexpected, surprising hydration induction postponement behavior as demonstrated through calorimetric testing. 1. A composition comprising: treated alkaline earth metal oxide particles treated by heating precursor alkaline earth metal oxide particles comprising 40-100 percent by total dry weight of calcium oxide , magnesium oxide , or mixture thereof , at an average temperature within 200° C.-700° C. , for a period of 20-300 minutes , in the presence of an organic material comprising a carbohydrate , amino-carboxylic acid , hydroxycarboxylic acid , or mixture thereof.2. The composition of wherein the treated alkaline earth metal oxide particles comprise at least 50 percent by total dry weight of calcium oxide based on total dry weight of the inorganic portion of particles; and the treated particles are treated by heating to 250° C.-500° C. for 20-200 minutes.3. The composition of wherein the treated alkaline earth metal oxide particles comprise at least 80-100 percent by total dry weight of calcium oxide based on total dry weight of the inorganic portion of the particles; and the treated particles were treated by heating to 250° C.-500° C. for 20-200 minutes.4. The composition of wherein the treated alkaline earth metal oxide particles claim 1 , after completion of heating claim 1 , have delayed onset of hydration of at least 30 minutes when the particles are mixed ...

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10-01-2019 дата публикации

CEMENT CLINKER LINE AND A METHOD FOR OPERATING A CEMENT CLINKER LINE

Номер: US20190010088A1
Автор: Leibinger Helmut
Принадлежит:

A method for manufacturing clinker includes sintering raw meal in a kiln to clinker, preheating the raw meal (prior to sintering the raw meal) in a preheater using a main flue gas stream from the kiln as heat source, dedusting the main flue gas downstream of the preheater at a temperature below the boiling point of mercury (thereby obtaining mercury loaded dust) and withdrawing a bypass flue gas stream from the kiln. The method is configured to efficiently remove mercury from the manufacturing process if mercury in the bypass flue gas is vaporized by injecting of at least a fraction of the mercury-loaded dust into the bypass flue gas stream. Subsequently, the bypass flue gas is dedusted and cooled down. Thereby, the mercury can be adsorbed by injecting an adsorbent (such as activated charcoal) into the bypass flue gas. With subsequent removal of the adsorbent, mercury is finally removed from the manufacturing process. 1. A method for manufacturing clinker , the method comprising:sintering raw meal in a kiln to clinker,preheating the raw meal in a preheater with the use of a main flue gas stream from the kiln as a heat source,dedusting the main flue gas stream at a location downstream from the preheater at a temperature below the boiling point of mercury, to obtain dedusted flue gas and mercury-loaded dust,withdrawing a bypass flue gas stream from the kiln,vaporizing at least one of mercury and a mercury compound in the bypass flue gas by injecting at least one of (i) a fraction of the mercury-loaded dust and (ii) a fraction of mercury-loaded waste-products into the bypass flue gas stream,dedusting the bypass flue gas stream,cooling the bypass flue gas stream to form a cooled bypass flues gas stream and binding at least one of the mercury and the mercury compound to an adsorbent, said adsorbent being injected into the cooled bypass flue gas stream,removing the adsorbent from the cooled bypass flue gas to form removed adsorbent and further processing the cooled bypass ...

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10-01-2019 дата публикации

CEMENT CLINKER LINE AND A METHOD FOR OPERATING A CEMENT CLINKER LINE

Номер: US20190010089A1
Автор: Leibinger Helmut
Принадлежит:

A method for manufacturing clinker including the steps of sintering raw meal in a kiln to clinker, preheating the raw meal in a preheater using a main flue gas stream from the kiln as a heat source, dedusting the main flue gas downstream from the preheater at a temperature below the boiling point of mercury, thereby obtaining mercury-loaded dust and withdrawing a bypass flue gas stream from the kiln. Implementation of the method results in efficient removal of the mercury from the process if mercury in the bypass flue gas is evaporated by injecting at least a fraction of the mercury-loaded dust into the bypass flue gas stream. Subsequently, the bypass flue gas is dedusted and cooled down. The mercury can be adsorbed by injecting an adsorbent like activated charcoal into the bypass flue gas. With the subsequent removal of the adsorbent, mercury is finally removed from the process. 1. A method for manufacturing clinker , the method comprising:sintering raw meal in a kiln to clinker,preheating raw meal in a preheater using a main flue gas stream from the kiln as a heat source,dedusting the main flue gas stream downstream from the preheater at a temperature below the boiling point of mercury to produce mercury-loaded dust,branching off an auxiliary flue gas stream from the main flue gas stream at an auxiliary flue gas stream branch prior to cooling the main flue gas stream to the temperature below the boiling point of mercury, wherein said branching is carried out either at a location downstream from the preheater or at an intermediate gas exit of the preheater,dedusting the auxiliary flue gas stream to obtain at least essentially mercury-free dust and dedusted auxiliary flue gas stream,binding mercury of the auxiliary flue gas stream to an adsorbent, wherein the binding comprises injecting the adsorbent into the dedusted auxiliary flue gas stream and cooling the auxiliary flue gas stream, andremoving the adsorbent from the dedusted auxiliary flue gas stream to form ...

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03-02-2022 дата публикации

Method and facility for producing material containing hydrated cement

Номер: US20220032316A1

A method for processing material that contains cement rock may involve comminuting the material in a first comminuting device, feeding the material to a reactor in which the material is mixed with an aqueous liquid and CO 2 and in which a mixing movement of the material is generated, and removing the material from the reactor and subdividing the material into at least two fractions by way of a classifying device. The temperature and the pressure in the reactor are maintained such that the pressure exceeds atmospheric pressure and such that the temperature is greater than 100° C. The method may further involve removing a withdrawal stream of the aqueous liquid from the reactor and separating and discharging suspended particles of the material from the withdrawal stream.

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03-02-2022 дата публикации

BIOMASS WASTE MATERIALS AS A SET-RETARDATION AGENT IN CEMENT OR CONCRETE

Номер: US20220033304A1
Принадлежит:

A concrete mixture is provided. The mixture includes cement powder, a plant biomaterial in a solid form, wherein the plant biomaterial does not comprise ash, and concrete aggregate, wherein a ratio of cement powder to the biomaterial ranges from 10:1 to 100:1. Methods of controlling concrete setting by adding a plant biomaterial in a solid form to a concrete mixture are also provided. 2. The concrete mixture of claim 1 , wherein the ratio of cement powder to the plant biomaterial ranges from 10:1 to 25:1.3. The concrete mixture of claim 1 , wherein the plant biomaterial is obtained from a plant selected from the group consisting of hemp claim 1 , kenaf claim 1 , and combinations thereof.4. The concrete mixture of claim 1 , wherein the plant biomaterial is obtained from a plant part selected from the group consisting of a stalk claim 1 , stem claim 1 , flowering material claim 1 , hurd claim 1 , bast claim 1 , and combinations thereof.5. The concrete mixture of claim 1 , wherein the solid form is selected from the group consisting of powder claim 1 , chips claim 1 , fibers claim 1 , and nanoparticles.6. The concrete mixture of claim 1 , wherein the mixture further comprises one or more materials selected from siliceous or calcareous fly ash claim 1 , slag cement claim 1 , and silica fume.7. A method of controlling concrete setting claim 1 , comprising adding a plant biomaterial in a solid form to a concrete mixture claim 1 , wherein the plant biomaterial does not comprise ash.8. The method of claim 7 , wherein the plant biomaterial replaces 1 to 10 wt % of cement powder in the concrete mixture.9. The method of claim 7 , wherein the plant biomaterial is obtained from a plant selected from the group consisting of hemp claim 7 , kenaf claim 7 , and combinations thereof.10. The method of claim 7 , wherein the plant biomaterial is obtained from a plant part selected from the group consisting of a stalk claim 7 , stem claim 7 , flowering material claim 7 , hurd claim 7 , ...

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19-01-2017 дата публикации

RECOVERY OF INTERMITTENT LOST HEAT

Номер: US20170015586A1
Автор: JORGET Serge
Принадлежит:

A cement clinker manufacturing method implemented in a continuous production facility having at least one fuel combustion area for firing an inorganic raw material into hot clinker, then the hot clinker is cooled in: a first cooling step in a first cooler; and a second consecutive cooling step in a second cooler. The first cooling step is continually carried out by blowing an oxygen gas on the hot clinker to obtain partially cooled clinker, and all the heated oxygen gas, created by the first cooler, is sent to the combustion area for use as combustion gas by adjusting the amount of oxygen gas, blown in the first cooler, such as to cover the combustion gas needs of the facility without any excess; and the partially cooled clinker is stored in a storage chamber, and the second cooling step is intermittently carried out on the partially cooled clinker. 11223345. Cement clinker manufacturing method implemented in a continuous production facility () having at least one fuel combustion zone ( , ′) for firing an inorganic raw material , in which the raw material is converted into clinker by firing , obtaining hot clinker () , the hot clinker () is then cooled in two successive steps , a first cooling step being carried out in a first cooler () and a second cooling step being carried out in a second cooler () ,wherein:{'b': 6', '7', '4', '2', '2, 'the first cooling step is carried out continuously by blowing an oxygenated gas () onto the hot clinker to obtain partially cooled clinker, and all heated oxygenated gas () output from the first cooler () is transferred to said at least one combustion zone (, ′) of said facility to be used as combustion gas by adjusting the amount of oxygenated gas blown in the first cooler so as to cover combustion gas needs of said facility without excess,'}{'b': 31', '5, 'the partially cooled clinker () is stored in a storage chamber of the second cooler () or a storage chamber associated with this second cooler, and the second cooling step on ...

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19-01-2017 дата публикации

CONCRETE MIX AND PRODUCTS INCLUDING RECYCLED PORCELAIN

Номер: US20170015587A1
Автор: Laurin Dale Paul
Принадлежит:

A concrete mix for use in forming molded concrete end products is disclosed. The concrete mix includes treated porcelain kernels, cement and sand. The treated porcelain kernels are formed from recycled and currently unusable porcelain products. The porcelain products are crushed and processed to create porcelain kernels having a desired size. The porcelain kernels having the desired size are mixed with cement and sand and the concrete mix is packaged for subsequent use. The concrete mix including the porcelain kernels formed from recycled porcelain products allows the porcelain end products to be recycled while providing concrete products that have lighter weight and greater flame resistance. 17-. (canceled)8. A method of forming a concrete mix , comprising the steps of:receiving a supply of recycled porcelain, wherein the recycled porcelain is obtained from recycled porcelain consumer products;processing the recycled porcelain to create finished porcelain kernels;mixing the finished porcelain kernels with at least cement and sand to create the concrete mix; andpackaging the concrete mix for use in forming an end product.9. The method of wherein the porcelain kernels have a size in the range between 0.0117″ to 0.750″.10. The method of wherein the treated porcelain kernels have a most preferred sizing between 0.265″ and 0.375″.11. The method of wherein the treated porcelain kernels constitute at least 35% of the concrete mix by weight.12. The method of wherein the cement includes fly ash and at least 30% of the packaged concrete mix by weight is formed from recycled porcelain and fly ash.1318-. (canceled) The present application is based on and claims priority to U.S. Provisional Patent Application Ser. No. 61/823,630 filed May 15, 2013, the disclosure of which is incorporated herein by reference.The present disclosure generally relates to a concrete mix that can be used in forming a variety of molded end products. More specifically, the present disclosure relates to ...

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18-01-2018 дата публикации

METHOD FOR REFINING OF IN POWER PLANTS PRODUCED COAL ASH AND COAL CONTAINING ASHES PRODUCED IN OTHER COMBUSTION PROCESSINGS

Номер: US20180015514A1
Принадлежит:

A method for industrial refining of coal ash created in power plants and carbonaceous ashes produced in other combustion processes by separating coal from said ashes and returning it to use and by recovering a substantially coal-free ash fraction obtained in the refining. In the method, coal ash and at least one ash fraction created by gasification technique in combustion plants are carefully proportioned in relation to one another and formed into a slurry mixture by means of an efficient dispersion technique, the slurry being then led to a flotation step, where a fraction rich in coal and a siliceous fraction poor in coal and a fraction dissolving in the process water are separated by flotation. The coal ash is arranged to have the highest proportion in the mixture to be taken to flotation, the ashes from combustion plants being dosed into said mixture in an amount that does not cause the maximum amounts of harmful substances to be exceeded in the qualities of the carbonaceous product and the silicate product poor in coal to be obtained. 1. A method for industrial refining of coal ash and carbonaceous ashes produced in other combustion processes of gasification plants by separating coal from said ashes and returning it to use and by recovering a substantially coal-free ash fraction obtained in the process , whereincoal ash and at least one ash fraction created by gasification technique in combustion plants are carefully proportioned in relation to one another and formed into a slurry mixture by means of an efficient dispersion technique, the mixture being then led to a flotation step, where a fraction rich in coal and a siliceous fraction poor in coal and a fraction dissolving in the process water are separated by flotation,the coal ash is arranged to have the highest proportion in the mixture to be taken to flotation, ash from combustion plants being dosed into said mixture in an amount that does not cause the maximum amounts of harmful substances to be exceeded ...

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21-01-2021 дата публикации

PROCESS FOR REFORMING THE FLY ASH AND APPARATUS THEREFOR

Номер: US20210017076A1
Принадлежит: TOKUYAMA CORPORATION

A process for reforming the fly ash, including the heating step that heats a raw fly ash powder containing the unburned carbon at a temperature of 780 to 1000° C. to decrease the amount of the unburned carbon contained in the raw fly ash powder; the classifying step that introduces the heat-treated fly ash containing the unburned carbon in decreased amounts obtained through the heating step into a classifying apparatus in the state of being heated at a high temperature so as to separate the fly ash into a coarse powder and a fine powder; the fine powder recovering step that recovers the fine powder of the heat-treated fly ash obtained through the classifying step by using a dust-collecting apparatus; and the milling step that mills the coarse powder of the heat-treated fly ash obtained through the classifying step until a 45 μm sieve residue becomes not more than 34% by mass, and then recovers the milled powder. 19.-. (canceled)10. A process for reforming a fly ash , including:a heating step that heats a raw fly ash powder containing an unburned carbon at a temperature of 780 to 1000° C. to decrease the amount of the unburned carbon contained in the raw fly ash powder;a classifying step that introduces the heat-treated fly ash containing the unburned carbon in decreased amounts obtained through said heating step into a classifying apparatus while conveying it maintaining a temperature of not lower than 400° C. so that the fly ash is separated into a coarse powder and a fine powder;a fine powder recovering step that recovers the fine powder of the heat-treated fly ash obtained through said classifying step by using a dust-collecting apparatus; anda milling step that mills the coarse powder of the heat-treated fly ash obtained through said classifying step until a 45 μm sieve residue becomes not more than 34% by mass, and then recovers a milled powder.11. The process for reforming the fly ash according to claim 10 , wherein the amount of the unburned carbon is ...

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21-01-2021 дата публикации

Organic fiber toughened inorganic composite artificial stone panel and preparation method thereof

Номер: US20210017770A1
Принадлежит:

An organic fiber toughened inorganic composite artificial stone panel and a preparation method thereof are disclosed. The panel includes a surface layer, an intermediate organic fiber toughened layer and a toughened base layer. The surface layer includes the following components: 40-70 parts of quartz sand, 20-30 parts of quartz powder, 20-45 parts of inorganic active powder, 0.5-4 parts of pigment, 0.1-3 part of water reducing agent and 3-10 parts of water. The intermediate organic fiber toughened layer includes the following components: 40-60 parts of inorganic active powder, 45-65 parts of sand, 0.8-1.5 parts of water reducing agent, 6-14 parts of water and 4-8 parts of organic fiber. The toughened base layer includes the following components: 30-50 parts of inorganic active powder, 30-55 parts of quartz sand, 15-20 parts of quartz powder, 0.5-1.2 parts of water reducing agent, 4-8 parts of water and 0.8-2.5 parts of toughener. 1. An organic fiber toughened inorganic composite artificial stone panel , comprising:a surface layer;an intermediate organic fiber toughened layer; anda toughened base layer,wherein the surface layer includes materials having the following components in parts by weight: quartz sand of 40 to 70 parts by weight, quartz powder of 10 to 30 parts by weight, inorganic active powder of 20 to 45 parts by weight, pigment of 0.5 to 4 parts by weight, water reducing agent of 0.3 to 1 part by weight and water of 3 to 10 parts by weight,wherein the intermediate organic fiber toughened layer includes materials having the following components in parts by weight: inorganic active powder of 40 to 60 parts by weight, sand of 45 to 65 parts by weight, water reducing agent of 0.8 to 1.5 parts by weight, water of 6 to 14 parts by weight and organic fiber of 0.5 to 1.2 parts by weight, andwherein the toughened base layer includes materials having the following components in parts by weight: inorganic active powder of 30 to 50 parts by weight, quartz sand of 30 ...

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22-01-2015 дата публикации

HYDRAULIC COMPOSITION WITH LOW CLINKER CONTENT

Номер: US20150020714A1
Принадлежит: LAFARGE

A hydraulic binder including in parts by mass: 1. A hydraulic binder comprising in parts by mass:(a) 40 to 70 parts of a Portland clinker;(b) 30 to 60 parts of fly ash;(c) optionally up to 30 parts of an inorganic material other than clinker or than fly ash;{'sub': '2', '(d) 2.5 to 15 parts of an alkali metal salt expressed in parts of equivalent-NaO relative to 100 parts of fly ash; and'}{'sub': '3', '(e) 2 to 14 parts of sulphate expressed in parts of SOrelative to 100 parts of clinker;'}the fly ash having a Dv97 less than or equal to 40 μm, and the sum of (a), (b) and (c) being equal to 100.2. The hydraulic binder according to claim 1 , wherein if the fly ash comprises more than 10% of reactive CaO claim 1 , then the fly ash has a Dv97 greater than or equal to 15 μm.3. The hydraulic binder according to claim 1 , wherein the fly ash comprises less than 10% of reactive CaO and/or a quantity of SiO+AlO+FeOgreater than 50%.4. The hydraulic binder according to claim 3 , wherein the fly ash comprises less than 10% of reactive CaO and/or a quantity of SiO+AlO+FeOgreater than 70%.5. The hydraulic binder according to claim 1 , wherein the alkali metal salt comprises sodium sulphate.6. A hydraulic composition claim 1 , comprising water and a hydraulic binder according to .7. A process for production of a hydraulic composition claim 1 , comprising mixing water and Portland clinker claim 1 , fly ash having a Dv97 less than or equal to 40 μm claim 1 , optionally an inorganic material other than clinker or than fly ash claim 1 , an alkali metal salt and sulphate in quantities as defined in .8. A shaped object for the construction field comprising a hydraulic binder according to . The invention relates to a hydraulic binder and a hydraulic composition with low clinker content, as well as to a process for preparation and uses of such a hydraulic composition.A known problem for hydraulic compositions is the high emission level of carbon dioxide during their production, and mainly ...

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22-01-2015 дата публикации

RECYCLED COMPOSITIONS FOR CONSTRUCTION, AND METHODS OF UTILIZING AND PRODUCING THE SAME

Номер: US20150021824A1
Принадлежит: FLASHFILL SERVICES, LLC

A low density annular grout composition for filling voids. The composition may consist of cementitious fly ash, water, set retarder and cellular foam. The composition may have a compressive strength of between 100 and 600 psi at seven days and less than 1500 psi at 28 days. The composition may have a density between 20 and 75 pcf. Also disclosed is a method of filling a void with a low density annular grout composition. The method can include determining the time necessary to fill the void, adding water and set retarder to a cementitious fly ash to make a wet mixture, adding air to the wet mixture, and adding the composition to the void. 1. A low density annular grout composition for filling voids comprising:between 30%-85% air by volume;between 50%-90% cementitious fly ash by weight;between 10% and 35% water by weight; andbetween 0.01% and 2% set retarder by weight,wherein the composition has compressive strength of between 100 and 600 psi at seven days, a compressive strength of less than 1500 psi at 28 days, and a density of between 20 and 75 pcf.2. The composition of claim 1 , wherein the air content of the composition is between 40% and 80% by volume of the composition.3. The composition of claim 1 , wherein the air content of the composition is less than 80% by volume of the composition.4. The composition of claim 1 , wherein the cementitious fly ash is between 60% and 80% by weight of the composition.5. The composition of claim 1 , wherein the cementitious fly ash is greater than 60% by weight of the composition.6. The composition of claim 1 , further comprising a filler between 1% and 45% by weight of the composition.7. The composition of claim 6 , wherein the filler is between 10% and 30% by weight of the composition.8. The composition of claim 6 , wherein the filler is a non-cementitious fly ash.9. The composition of claim 8 , wherein the water to fly ash ratio in the composition is between 0.15 to 0.40.10. The composition of claim 9 , wherein the water to ...

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28-01-2016 дата публикации

NOVEL SULFO-ALUMINOUS CLINKER WITH A LOW BELITE CONTENT

Номер: US20160023947A1
Принадлежит:

The present invention relates to a new sulfo-aluminate based clinker with a low belite content, a method for preparing this clinker, as well as the use of the clinker for preparing a hydraulic binder, and later on, grout, concrete or mortar. 1. A sulfo-aluminate based clinker , the phase composition of which comprises , with respect to the total weight of the clinker:{'sub': 4', 'x', 'y', 'z, 'from 20 to 90 % of a calcium sulfoaluminate phase corresponding to the formula CAF$, withx varying from 2 to 3,y varying from 0 to 0.5,and z varying from 0.8 to 1.2;{'sub': 6', 'x′', 'y′, 'from 0 to 25 % of a calcium aluminoferrite phase the composition of which corresponds to the general formula CAF, with x′ varying from 0 to 1.5 and y′ varying from 0.5 to 3; and'}{'sub': '2', 'less than 20 % belite CS phase; and'}{'sub': 11', '4, 'less than 2 % of a CSB phase;'}2. The clinker according to claim 1 , wherein it contains from 30 to 80% of an iron-doped calcium sulfo-aluminate phase CAF$.3. The clinker according to claim 1 , wherein x varies from 2.1 to 2.9 and/or y varies from 0.05 to 0.5.4. The clinker according to claim 1 , wherein it contains from 0 to 20% of a calcium aluminoferrite phase CAF.5. The clinker according to claim 1 , wherein x′ varies from 0.65 to 1.3 and/or y′ varies from 1.5 to 1.5 to 2.5.6. The clinker according to claim 1 , wherein it contains less than 1% CSB phase.7. The clinker according to claim 1 , it contains less than 15% CS belite phase.8. The clinker according to claim 1 , wherein it contains less than 3% CaOl.9. The clinker according to claim 1 , wherein it contains less than 5% C$.10. The clinker according to claim 1 , wherein it contains less than 10% CAS.11. A method for preparing a clinker according to comprising the following steps: [{'sub': '2', 'from 0.1 to 40% bauxite, marlstones, red muds and/or any other sedimentary, metamorphic or magmatic rocks or industrial mineral derivatives with a high aluminum content and a SiOcontent less than 20 ...

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24-04-2014 дата публикации

Process and plant for producing cement clinker and for purifying the offgases formed

Номер: US20140109800A1
Автор: Franz-Josef Zurhove
Принадлежит: ELEX CEMCAT AG

The invention relates to a process and a plant for producing cement clinker and for purifying the off-gases formed thereby, wherein cement raw meal is preheated in a preheater by means of hot off-gases and then optionally precalcined, the preheated and optionally precalcined cement raw meal is burnt in a rotary kiln to form cement clinker, the cement clinker is cooled in a cooler, the hot off-gases used in the preheater are used in a raw mill for treating the cement raw meal, the dust content of a dust-containing mill off-gas thereby formed is reduced in a separating device to less than 5 g/Nm 3 , preferably less than 1 g/Nm 3 , alkali hydrogen carbonate and/or alkali carbonate is added to and mixed with the mill off-gas whose dust content has been reduced to less than 5 g/Nm 3 , and the mixed gas thereby formed is subsequently fed to a process filter for separation of dust laden with pollutants.

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24-04-2014 дата публикации

METHOD AND DEVICE FOR REMOVING MERCURY DURING THE PRODUCTION OF CEMENT CLINKER

Номер: US20140109807A1
Принадлежит: SCHEUCH GMBH

A method and a device remove mercury from exhaust gases during a production of cement clinker. The device contains a pre-heating stage, a feed point for raw materials required for the production of the cement clinker, a rotary kiln for burning the raw materials, a filter stage for removing dust from the exhaust gases conducted in the main flow, and a raw mix mill for partially mill drying the raw materials. A circuit for the mercury in the exhaust gases is formed between the pre-heating stage and the raw mix mill or the filter stage. To achieve good mercury removal at low cost, a sub-flow of 1 to 30 volume percent of the exhaust gases is branched off from the main flow of the exhaust gases having a temperature of at least 300° C. A separator and thereafter at least one stage for removing mercury are arranged in the sub-flow. 134-. (canceled)35. A method for separating mercury from exhaust gases during production of cement clinker , which comprises the steps of:feeding in raw materials, required for producing the cement clinker, into a pre-heating stage against a direction of flow of the exhaust gases according to a counter flow principle, and the mercury bonded in the raw materials is vaporized due to a heating of the raw materials in the pre-heating stage;firing the raw material in a rotary kiln;using the exhaust gases conducted in a main flow for at least partially mill drying the raw materials in at least one raw mix mill;dedusting the exhaust gases in at least one filter stage before the exhaust gases escape into atmosphere;feeding dust separated in the at least one filter stage into the pre-heating stage at least partially together with a milled raw material;forming a circuit for the mercury in the exhaust gases between the pre-heating stage and the raw mix mill or the at least one filter stage; andbranching off from the main flow of the exhaust gases a sub-flow of 1 to 30 per cent by volume of the exhaust gases having a temperature of at least 300° C., and the ...

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24-01-2019 дата публикации

U-Shaped Seal and Method for Use in Cement Plants

Номер: US20190024976A1
Принадлежит:

A method to thermally convert alternative fuels within a loop seal reactor by utilizing preheated/calcined cement meal as the heat source within which alternative fuels are immersed, subjected to drying, pyrolysis and subsequently charred, and an apparatus utilized to practice such method. 1. An apparatus for the heat treatment of solid combustible fuel comprising a hollow tubular structure having at least two substantially vertically extending hollow conduits comprising a first conduit adapted to have particulate material pass downward there through and a second conduit adapted to have particulate material pass upward there through , with each of the first and second conduits having a lower end , with each lower end attached to opposite ends of a bottom hollow third conduit that is adapted to have particulate material pass there through from the lower end of the first conduit to lower end of the second conduit , wherein the tubular structure further comprises a means to direct a pulsed gas upward from beneath the third conduit into the interior of at least one of the vertically extending conduits for a duration ranging from about 10 to about 200 ms , an amplitude ranging from about 0.2 to about 5 bar and a frequency ranging from about 0.1 to about 10 hz.2. The apparatus of wherein the third conduit is a straight conduit that extends at a downward slope from the lower end of the first conduit to the lower end of the second conduit.3. The apparatus of wherein the third conduit further comprises means for segregating heavy objects in a bottom part of the third conduit.4. The apparatus according to wherein the apparatus further comprises a calciner for calcining cement meal that is provided to the hollow tubular structure and for receiving charred combustible waste from the hollow tubular structure.5. A method for the heat treatment of combustible waste during a process for the manufacture of cement clinker where cement raw meal is preheated and calcined in a preheater ...

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28-01-2021 дата публикации

CEMENT SLURRIES, CURED CEMENT AND METHODS OF MAKING AND USE THEREOF

Номер: US20210024414A1
Принадлежит: Saudi Arabian Oil Company

Cured cements, cement slurries, and methods of making cured cement and methods of using cement slurries are provided. The method of making a cured cement comprising: synthesizing nanomaterials via chemical vapor deposition on at least one of cement particles or cement additive particles to form nanomaterial particles, adding the nanomaterial particles to a cement slurry to form a modified cement slurry, and curing the modified cement slurry to form a cured cement, in which the nanomaterials are interconnected and form a conductive web within the cured cement. 1. A method of making a cured cement comprising:synthesizing nanomaterials via chemical vapor deposition on at least one of cement particles or cement additive particles to form nanomaterial particles,adding the nanomaterial particles to a cement slurry to form a modified cement slurry, andcuring the modified cement slurry to form a cured cement, in which the nanomaterials are interconnected and form a conductive web within the cured cement.2. The method of claim 1 , further comprising adding at least one of a dispersing agent or a surfactant to the cement slurry prior to adding the nanomaterial particles to the cement slurry.3. The method of claim 2 , in which the dispersing agent comprises polycarboxylate ether.4. The method of claim 2 , in which the surfactant comprises at least one of anionic surfactants claim 2 , cationic surfactants claim 2 , amphoteric surfactants claim 2 , zwitterionic surfactants claim 2 , nonionic surfactants claim 2 , or combinations thereof.5. The method of claim 1 , further comprising functionalizing the nanomaterials with at least one of magnetic or electric properties prior to adding the nanomaterial particles to the cement slurry.6. The method of claim 1 , in which the nanomaterials comprise at least one of nanotubes claim 1 , nanofibers claim 1 , or nanosheets.7. The method of claim 1 , in which the nanomaterials comprise at least one of nanosilica claim 1 , nanoalumina claim 1 ...

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02-02-2017 дата публикации

Method for controlling nox concentration in exhaust gas in combustion facility using pulverized coal

Номер: US20170029328A1
Принадлежит: Mitsubishi Materials Corp

A method for controlling an NOx concentration in an exhaust gas in a combustion facility by: measuring a reaction velocity k i of each of a plurality of chars, each corresponding to a plurality of types of pulverized coals; determining a relationship between the NOx concentration in the exhaust gas and the reaction velocity k i for each of the chars; (iii) blending the plurality of the types of the pulverized coal, wherein a blending ratio of the plurality of the types of the pulverized coal is determined by using, as an index, a reaction velocity k blend of the char of the blended pulverized coal, which corresponds to a target NOx concentration or below, on the basis of the relationship; and supplying the blended pulverized coal to the combustion facility as the fuel of the combustion facility.

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02-02-2017 дата публикации

QUICK-DRYING BUILDING MATERIAL COMPOSITION BASED ON A MINERAL HYBRID BINDER

Номер: US20170029333A1
Принадлежит: SIKA TECHNOLOGY AG

A quick-drying gypsum composition, in particular for use as gypsum filling compound and for the production of floor coverings, wherein the gypsum composition contains 20 to 70% of a mixture of calcium aluminate and calcium sulfate hemihydrate and/or anhydrite and/or calcium sulfate dihydrate as hydraulic binders and 30 to 80% by weight of fillers, and wherein the weight ratio of calcium aluminate to calcium sulfate hemihydrate and/or anhydrite and/or calcium sulfate dihydrate binders lies in the range from 1:1 to 1:5. Gypsum compositions of this type are characterized by a particularly beneficial shrinkage behavior, such that stresses and cracks in the dried composition can be avoided. At the same time, the gypsum compositions dry to readiness for covering in a time that is compatible with conventional cement filling compounds. 2. The gypsum composition as claimed in claim 1 , wherein the weight ratio of calcium aluminate to calcium sulfate hemihydrate and/or anhydrite and/or calcium sulfate dihydrate binder is in the range from 1:1.6 to 1:4.3. The gypsum composition as claimed in claim 1 , comprises 20 to 60 wt % claim 1 , of the mixture of calcium aluminate and calcium sulfate hemihydrate and/or anhydrite and/or calcium sulfate dihydrate binder.4. The gypsum composition as claimed in claim 1 , comprises fillers in the form of sand and calcium carbonate and/or finely ground limestone.5. The gypsum composition as claimed in claim 1 , wherein it has a fillers content of 35 to 75 wt %.6. The gypsum composition as claimed in claim 1 , further comprises a lithium salt.7. The gypsum composition as claimed in claim 6 , comprises lithium salts.8. The gypsum composition as claimed in claim 1 , further comprises tartaric acid and/or a tartaric salt.9. The gypsum composition as claimed in claim 8 , comprises tartaric acid or and/or a tartaric salt in an amount of 0.15 to 0.005 wt %.10. The gypsum composition as claimed in claim 1 , wherein it comprises additional additives ...

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