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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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Мониторинг СМИ

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

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Применить Всего найдено 9. Отображено 8.
25-05-2017 дата публикации

SELECTIVITY OF IONIC LIQUID ALKYLATION

Номер: US20170144141A1
Принадлежит:

A method of controlling a hydrocarbon conversion process is described. The method involves introducing a reactant into a reaction zone containing an ionic liquid catalyst. The reaction zone has at least two zones. The mass transfer resistance in the second zone is greater than the mass transfer resistance in the first zone. 1. A method of controlling a hydrocarbon conversion process comprising:introducing a reactant into a reaction zone containing an ionic liquid catalyst comprising ionic liquid droplets, the reaction zone having at least two zones, the first zone having a first mass transfer resistance in the ionic liquid droplets and the second zone having a second mass transfer resistance in the ionic liquid droplets greater than the first mass transfer resistance.2. The method of wherein the second mass transfer resistance is greater than the first mass transfer resistance by changing the first mass transfer resistance claim 1 , the second mass transfer resistance claim 1 , or both.3. The method of wherein the first mass transfer resistance claim 2 , the second mass transfer resistance claim 2 , or both are changed by changing a size of droplets of the ionic liquid in the second zone compared to a size of droplets of the ionic liquid catalyst in the first zone.4. The method of wherein the size of the droplets of ionic liquid in the second zone is changed by increasing a shear rate of the first zone claim 3 , decreasing a shear rate of the second zone claim 3 , or both.5. The method of wherein the size of the droplets of the ionic liquid in the second zone is greater than the size of the droplets in the second zone.6. The method of wherein the size of the droplets of the ionic liquid is changed using a static mixer designed to increase the size of the droplets of the ionic liquid in the second zone compared to the size of the droplets of the ionic liquid in the first zone.7. The method of wherein the first mass transfer resistance claim 1 , the second mass ...

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14-11-2017 дата публикации

Selectivity of ionic liquid alkylation

Номер: US0009815049B2
Принадлежит: UOP LLC

A method of controlling a hydrocarbon conversion process is described. The method involves introducing a reactant into a reaction zone containing an ionic liquid catalyst. The reaction zone has at least two zones. The mass transfer resistance in the second zone is greater than the mass transfer resistance in the first zone.

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10-05-2018 дата публикации

PROCESSES AND SYSTEMS FOR CONTROLLING COOLING FLUID IN AN IONIC LIQUID REACTOR SYSTEM WITH A HEAT EXCHANGER

Номер: US20180128560A1
Принадлежит:

Processes for controlling the rate and temperature of cooling fluid through a heat exchange zone in, for example, an alkylation reactor using an ionic liquid catalyst. A cooling fluid system may be used to provide the cooling fluid which includes a chiller and a reservoir. The cooling fluid may pass from the reservoir through the heat exchange zone. A bypass line may be used to pass a portion of the cooling fluid around the heat exchange zone. The amount of cooling fluid may be adjusted, with a valve, based upon the temperature of the cooled process fluid flowing out of the heat exchange zone. Some of the cooling fluid from the chiller may be circulated back to the chiller in a chiller loop. 1. A process for controlling a flow of a cooling fluid through a heat exchanger , the process comprising:passing a cooling fluid from a chilling zone to a reservoir;passing a first portion of the cooling fluid from the reservoir through a heat exchange zone;passing a second portion of the cooling fluid from the reservoir through a bypass line around the heat exchange zone;passing a process fluid through the heat exchange zone; and,absorbing heat from the process fluid with the cooling fluid in the heat exchange zone to provide a cooled process fluid.2. The process of for comprising: adjusting the second portion of the cooling fluid from the reservoir that flows through a bypass line based upon a temperature of the cooled process fluid.3. The process of wherein a temperature of the first portion of the cooling fluid from the reservoir is between approximately −6.7 to 26.7° C. (20 to 80° F.).4. The process of wherein a temperature of the first portion of the cooling fluid from the reservoir is between approximately 1.7 to 12.8° C. (35 to 55° F.).5. The process of wherein the heat exchange zone comprises a plurality of heat exchangers.6. The process of wherein a first heat exchanger from the plurality of heat exchangers receives a process fluid from a first reaction zone claim 5 , ...

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20-09-2018 дата публикации

Reactor system for use with an ionic liquid catalyst

Номер: US20180264431A1
Принадлежит: UOP LLC

Reactor systems for use with ionic liquid catalyst. The reactor systems include one or more stages, which include a reactor and a heat exchanger, and a separation zone. The reactor and the heat exchanger may have a vertical orientation. Additionally, a separation vessel may also include a vertical orientation. The heat exchanger may allow for linear flow of process fluid to control residence time.

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06-10-2016 дата публикации

Heat exchanger for use in alkylation process using halometallate ionic liquid micro-emulsions

Номер: WO2016161204A1
Принадлежит: UOP LLC

An ionic liquid reaction zone and an alkylation process utilizing the ionic liquid reaction zone are described. The reaction zone comprises at least one shell and tube heat exchanger bundle. The heat exchanger bundle has a shell side and a tube side, and it has an isoparaffin inlet, an olefin inlet, and a product outlet. The tube side has at least one tube. Each tube has an inlet at one end and an outlet at the opposite end. There are at least two inlets along the length of the at least one tube. The olefin inlet is in fluid communication with the at least two inlets along the length of the at least one tube.

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29-10-2019 дата публикации

Processes and systems for controlling cooling fluid

Номер: CA2981120C
Принадлежит: UOP LLC

Processes for controlling the rate and temperature of cooling fluid through a heat exchange zone in, for example, an alkylation reactor using an ionic liquid catalyst. A cooling fluid system may be used to provide the cooling fluid which includes a chiller and a reservoir. The cooling fluid may pass from the reservoir through the heat exchange zone. A bypass line may be used to pass a portion of the cooling fluid around the heat exchange zone. The amount of cooling fluid may be adjusted, with a valve, based upon the temperature of the cooled process fluid flowing out of the heat exchange zone. Some of the cooling fluid from the chiller may be circulated back to the chiller in a chiller loop.

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22-12-2016 дата публикации

Processes and systems for controlling cooling fluid

Номер: CA2981120A1
Принадлежит: UOP LLC

Processes for controlling the rate and temperature of cooling fluid through a heat exchange zone in, for example, an alkylation reactor using an ionic liquid catalyst. A cooling fluid system may be used to provide the cooling fluid which includes a chiller and a reservoir. The cooling fluid may pass from the reservoir through the heat exchange zone. A bypass line may be used to pass a portion of the cooling fluid around the heat exchange zone. The amount of cooling fluid may be adjusted, with a valve, based upon the temperature of the cooled process fluid flowing out of the heat exchange zone. Some of the cooling fluid from the chiller may be circulated back to the chiller in a chiller loop.

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07-12-2022 дата публикации

Processes and systems for controlling cooling fluid

Номер: EP3310471B1
Принадлежит: UOP LLC

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