RU2009104699A - Реакторная установка с извлечением промежуточного продукта - Google Patents

Реакторная установка с извлечением промежуточного продукта Download PDF

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RU2009104699A
RU2009104699A RU2009104699/05A RU2009104699A RU2009104699A RU 2009104699 A RU2009104699 A RU 2009104699A RU 2009104699/05 A RU2009104699/05 A RU 2009104699/05A RU 2009104699 A RU2009104699 A RU 2009104699A RU 2009104699 A RU2009104699 A RU 2009104699A
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annular
catalytic chamber
installation
reactor
annular catalytic
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Андреа Дж. БОДЗАНО (US)
Андреа Дж. Бодзано
Том Нельсон КЭЛЬНЕЗ (US)
Том Нельсон КЭЛЬНЕЗ
Карл Дж. СТИВЕНС (US)
Карл Дж. СТИВЕНС
Стивен М. ПОКЛОП (US)
Стивен М. ПОКЛОП
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Юоп Ллк (Us)
Юоп Ллк
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    • B01J2208/00106Controlling the temperature by indirect heat exchange
    • B01J2208/00168Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
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    • Y10S585/00Chemistry of hydrocarbon compounds
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract

1. Реакторная установка (10), содержащая: ! несколько реакторов (12), соединенных друг с другом и содержащих, по меньшей мере, одну пару реакторов (12а, b), разделенных промежуточным местом (33); ! магистраль (25) подачи сырья, предназначенную для подачи сырьевого потока реагентов на вход (21а, b) более одного из указанных нескольких реакторов (12а, b); и ! отводящее устройство (30), соединенное с промежуточным местом (33) и способное направлять первую часть потока (32а) продукта, вышедшего из первого реактора (12а) указанной пары реакторов (12а, b), в первое место (40) и направлять вторую часть потока продукта на вход (21b) другого реактора (12b) указанной пары реакторов (12а, b). ! 2. Установка (10) по п.1, в которой первый реактор (12а) из нескольких реакторов (12а, b) содержит первую кольцеобразную каталитическую камеру (56а), а второй реактор (12b) из нескольких реакторов (12а, b) содержит вторую кольцеобразную каталитическую камеру (58а) и первая кольцеобразная каталитическая камера (56а) концентрически расположена внутри второй кольцеобразной каталитической камеры (58а). ! 3. Установка (10) по п.2, которая дополнительно содержит первую кольцеобразную камеру (60) сбора, расположенную между первой кольцеобразной каталитической камерой (56а) и второй кольцеобразной каталитической камерой (58а) и вторую кольцеобразную камеру (62) сбора, расположенную вокруг второй кольцеобразной каталитической камеры (58а). ! 4. Установка (10) по п.2, в которой выходящий поток (32а) первой кольцеобразной каталитической камеры (56а) подают во вторую кольцеобразную каталитическую камеру (58а). ! 5. Установка (10) по п.3, в которой магистраль (25) подачи сырья соединена с первым входом (21а) в первую кольцео�

Claims (10)

1. Реакторная установка (10), содержащая:
несколько реакторов (12), соединенных друг с другом и содержащих, по меньшей мере, одну пару реакторов (12а, b), разделенных промежуточным местом (33);
магистраль (25) подачи сырья, предназначенную для подачи сырьевого потока реагентов на вход (21а, b) более одного из указанных нескольких реакторов (12а, b); и
отводящее устройство (30), соединенное с промежуточным местом (33) и способное направлять первую часть потока (32а) продукта, вышедшего из первого реактора (12а) указанной пары реакторов (12а, b), в первое место (40) и направлять вторую часть потока продукта на вход (21b) другого реактора (12b) указанной пары реакторов (12а, b).
2. Установка (10) по п.1, в которой первый реактор (12а) из нескольких реакторов (12а, b) содержит первую кольцеобразную каталитическую камеру (56а), а второй реактор (12b) из нескольких реакторов (12а, b) содержит вторую кольцеобразную каталитическую камеру (58а) и первая кольцеобразная каталитическая камера (56а) концентрически расположена внутри второй кольцеобразной каталитической камеры (58а).
3. Установка (10) по п.2, которая дополнительно содержит первую кольцеобразную камеру (60) сбора, расположенную между первой кольцеобразной каталитической камерой (56а) и второй кольцеобразной каталитической камерой (58а) и вторую кольцеобразную камеру (62) сбора, расположенную вокруг второй кольцеобразной каталитической камеры (58а).
4. Установка (10) по п.2, в которой выходящий поток (32а) первой кольцеобразной каталитической камеры (56а) подают во вторую кольцеобразную каталитическую камеру (58а).
5. Установка (10) по п.3, в которой магистраль (25) подачи сырья соединена с первым входом (21а) в первую кольцеобразную каталитическую камеру (56а) и соединена со вторым входом (21b) во вторую кольцеобразную каталитическую камеру (58а).
6. Установка (10) по п.1, в которой первое место является участком (40) восстановления продукта, который способен разделять компоненты продукта.
7. Установка (10) по п.2, в которой третий реактор (12с) из нескольких реакторов (12) содержит третью кольцеобразную каталитическую камеру (56b) и четвертый реактор (12d) из нескольких реакторов (12) содержит четвертую кольцеобразную каталитическую камеру (58b) и катализатор может течь из первой кольцеобразной каталитической камеры (56а) в третью кольцеобразную каталитическую камеру (56b) и из второй кольцеобразной каталитической камеры (58а) в четвертую кольцеобразную каталитическую камеру (58b).
8. Установка (10) по п.7, в которой магистраль (25) подачи сырья питает трубу (70), которая содержит проницаемую для текучей среды стенку (65), соединенную с указанной первой кольцеобразной каталитической камерой (56а).
9. Установка (10) по п.8, в которой магистраль (25) подачи сырья дополнительно питает распределительную магистраль (23), соединенную с указанной второй кольцеобразной каталитической камерой (58а).
10. Установка (10) по п.9, в которой труба (70) проходит через распределительную магистраль (23).
RU2009104699/05A 2006-07-12 2007-06-15 Реакторная установка с извлечением промежуточного продукта RU2444402C2 (ru)

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CN101489662B (zh) 2012-08-08
US7807114B2 (en) 2010-10-05
EP2038374A2 (en) 2009-03-25
JP5491861B2 (ja) 2014-05-14
WO2008008597A3 (en) 2008-03-06
US20090324463A1 (en) 2009-12-31
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US7582268B1 (en) 2009-09-01
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