WO2014200383A1 - Installation for activating phase separation process - Google Patents
Installation for activating phase separation process Download PDFInfo
- Publication number
- WO2014200383A1 WO2014200383A1 PCT/RU2013/000486 RU2013000486W WO2014200383A1 WO 2014200383 A1 WO2014200383 A1 WO 2014200383A1 RU 2013000486 W RU2013000486 W RU 2013000486W WO 2014200383 A1 WO2014200383 A1 WO 2014200383A1
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- Prior art keywords
- module
- collector
- modules
- installation
- reaction chambers
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/025—High gradient magnetic separators
- B03C1/031—Component parts; Auxiliary operations
- B03C1/032—Matrix cleaning systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/23—Magnetic separation acting directly on the substance being separated with material carried by oscillating fields; with material carried by travelling fields, e.g. generated by stationary magnetic coils; Eddy-current separators, e.g. sliding ramp
- B03C1/24—Magnetic separation acting directly on the substance being separated with material carried by oscillating fields; with material carried by travelling fields, e.g. generated by stationary magnetic coils; Eddy-current separators, e.g. sliding ramp with material carried by travelling fields
Definitions
- the invention relates to installations in which the principle of a traveling or rotating electromagnetic field is used to activate physico-chemical and mechano-physical processes, and the principle of centrifugal devices is used to separate phases.
- the invention can be used in the forest, chemical and other industries for the treatment of wastewater from industrial and agricultural enterprises, including domestic wastewater.
- a known installation for activating processes and phase separation (patent RU JY22049562, IPC: VO ⁇ 1 / 24, B01J8 / 16, claimed June 23, 1992, published December 10, 1995), containing coaxially mounted modules in the form of tubular reaction chambers filled with ferromagnetic particles and placed in a housing formed by the walls of two concentrically arranged cylinders.
- Each reaction chamber is provided with a rotating magnetic field inductor surrounding it.
- the input ends of the reaction chambers in each module are connected to an annular distributing collector, and their output ends are located tangentially to the wall of the inner cylinder forming the cavity of the collecting chamber of the module.
- the collecting chambers of all modules are interconnected to form a single channel.
- a disadvantage of the known installation is the low productivity of phase separation, which is associated with an insufficiently effective effect of centrifugal forces and the formation of a single flow front from the collecting chambers in the channel uniting the collecting chambers.
- the collector may have a rotational movement of the flow, which also reduces the performance of the installation and may cause the collector to overheat.
- the problem solved by the claimed invention is to increase the efficiency of the action of centrifugal forces on the heterogeneous mixture of the processed stream to increase the efficiency of phase separation, as well as preventing overheating of the distributing collectors.
- each reaction chamber is equipped with a rotating magnetic inductor enclosing it the fields, the input ends of the reaction chambers in each module are connected to the annular distributing collector, and their output ends are located tangentially on the inner cylinder, which forms the cavity of its collecting chamber, while the collecting chambers of all the modules are interconnected to form a single channel, each module is shifted around its axis by 20-30 ° relative to the module located above, and the annular distributing module collector is made in the form of a toroid, cut at the pipe connecting the collector to the supply line, and the ends of the collector are hermetically closed.
- figure 1 schematically shows an installation consisting of seven modules; 2 and FIG. 3 show a module with eight reaction chambers; figure 4 - arrangement of two contacting modules.
- the installation contains the estimated number of coaxially mounted modules 1, each of which is shifted around the axis with respect to the overlying module by 20-30 °.
- Each module 1 has an annular distributing manifold 2 in the form of a toroid, cut off at the pipe 3 connecting it with a flange 4 to a common supply line 5.
- the free ends of the annular distributing collector 2 are hermetically closed.
- the housing of module 1 is formed by the walls of two concentrically mounted cylinders - the inner 6 and outer 7 and has a bottom 8 and a cover 9.
- the cavity of the inner cylinder 6 forms a collecting tank of module 1, and the connected collecting tanks of several modules 1 form a common collecting tank 10.
- tubular reaction chambers 11 with ferromagnetic particles (not shown) are installed, on each of which an inductor of a rotating magnetic field 12 is fixed.
- the output ends of the reaction chambers 11 are connected by tangential nozzles 13 with the wall of the inner cylinder 6.
- the input ends of the reaction chambers 11 are connected with branch pipes 14, and those - with an annular distributing manifold 2.
- the module 1 is also provided with fitting 15 for entering the cooling agent and the fitting 16 for its removal. To ensure the circular movement of the refrigerant in each module 1 between the fittings 15 and 16, a blind partition 17 is installed.
- the installation contains an additional chamber 18 in the form of a hollow cylinder connected to the collecting tank 10, a hollow cone 19, a sludge collector 20, and also a drain pipe 21, a discharge pipe 22 filter system 23, a pipe for the removal of pure product 24, and tanks 25 for additives, 85 connected to a common supply line 5.
- Installation works as follows. The cooling system of the inductors 12 is turned on, then the inductors 12 are fed and at the same time the initial product is fed into the reaction chambers 11 from the collectors 2. The collectors 2 are made open
- the installation shown in FIG. 1 contains seven modules, each of which contains eight inductors, and has a capacity of about 120 m 3 / h. Each module works independently of the others and can contain up to twelve reaction chambers with a total capacity of up to 250 m 3 / h. Performance
- Installation software can be enhanced by adding new modules. So the installation performance with ten modules can reach up to 2500 m 3 / h.
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
Description
УСТАНОВКА ДЛЯ АКТИВАЦИИ ПРОЦЕССА РАЗДЕЛЕНИЯ ФАЗ INSTALLATION FOR ACTIVATION OF THE PHASE SEPARATION PROCESS
Изобретение относится к установкам, в которых для активации физико-химических и механо-физических процессов используют принцип бегущего или вращающегося электромагнитного поля, а для разделения фаз - принцип аппаратов центробежного типа. Изобретение может быть использовано в лесной, химической и других отраслях промышленности для обезвреживания сточных вод промышленных и сельскохозяйственных предприятий, в том числе бытовых сточных вод. The invention relates to installations in which the principle of a traveling or rotating electromagnetic field is used to activate physico-chemical and mechano-physical processes, and the principle of centrifugal devices is used to separate phases. The invention can be used in the forest, chemical and other industries for the treatment of wastewater from industrial and agricultural enterprises, including domestic wastewater.
Известна установка для активации процессов и разделения фаз (патент RU JY22049562, МПК: ВОЗС1/24, B01J8/16, заявлено 23.06.1992г., опубликовано 10.12.1995г.), содержащая соосно установленные модули в виде трубчатых реакционных камер, заполненных ферромагнитными частицами и размещенных в корпусе, образованном стенками двух концентрично расположенных цилиндров. Каждая реакционная камера снабжена охватывающим ее индуктором вращающегося магнитного поля. Входные концы реакционных камер в каждом модуле соединены с кольцевым раздающим коллектором, а их выходные концы расположены тангенциально стенке внутреннего цилиндра, образующего полость собирающей камеры модуля. Собирающие камеры всех модулей соединены между собой с образованием единого канала. Недостатком известной установки является невысокая производительность разделения фаз, что связано с недостаточно эффективным воздействием центробежных сил и образованием вследствие этого в канале, объединяющем собирающие камеры, единого фронта потока от собирающих камер. Кроме того, в кольцевом раздающем коллекторе возможно вращательное движение потока, что также снижает производительность установки и может вызвать перегрев коллектора. A known installation for activating processes and phase separation (patent RU JY22049562, IPC: VOС1 / 24, B01J8 / 16, claimed June 23, 1992, published December 10, 1995), containing coaxially mounted modules in the form of tubular reaction chambers filled with ferromagnetic particles and placed in a housing formed by the walls of two concentrically arranged cylinders. Each reaction chamber is provided with a rotating magnetic field inductor surrounding it. The input ends of the reaction chambers in each module are connected to an annular distributing collector, and their output ends are located tangentially to the wall of the inner cylinder forming the cavity of the collecting chamber of the module. The collecting chambers of all modules are interconnected to form a single channel. A disadvantage of the known installation is the low productivity of phase separation, which is associated with an insufficiently effective effect of centrifugal forces and the formation of a single flow front from the collecting chambers in the channel uniting the collecting chambers. In addition, in the ring distributor the collector may have a rotational movement of the flow, which also reduces the performance of the installation and may cause the collector to overheat.
Задачей, решаемой заявляемым изобретением, является повышение эффективности воздействия центробежных сил на гетерогенную смесь обрабатываемого потока для повышения эффективности разделения фаз, а также предотвращение перегрева раздающих коллекторов. The problem solved by the claimed invention is to increase the efficiency of the action of centrifugal forces on the heterogeneous mixture of the processed stream to increase the efficiency of phase separation, as well as preventing overheating of the distributing collectors.
Поставленная задача решается тем, что в установке для активации процессов и разделения фаз, содержащей соосно установленные модули в виде трубчатых реакционных камер, заполненных ферромагнитными частицами и размещенных в корпусе, образованном стенками двух концентрично расположенных цилиндров, причем каждая реакционная камера снабжена охватывающим ее индуктором вращающегося магнитного поля, входные концы реакционных камер в каждом модуле соединены с кольцевым раздающим коллектором, а их выходные концы расположены тангенциально стенке внутреннего цилиндра, образующего полость его собирающей камеры, при этом собирающие камеры всех модулей соединены между собой с образованием единого канала, каждый модуль сдвинут вокруг оси на 20-30° относительно модуля, расположенного выше, а кольцевой раздающий коллектор модуля выполнен в виде тороида, разрезанного у патрубка, соединяющего коллектор с подводящей магистралью, причем концы коллектора герметично закрыты. The problem is solved in that in the installation for the activation of processes and phase separation, containing coaxially mounted modules in the form of tubular reaction chambers filled with ferromagnetic particles and placed in a housing formed by the walls of two concentrically arranged cylinders, each reaction chamber is equipped with a rotating magnetic inductor enclosing it the fields, the input ends of the reaction chambers in each module are connected to the annular distributing collector, and their output ends are located tangentially on the inner cylinder, which forms the cavity of its collecting chamber, while the collecting chambers of all the modules are interconnected to form a single channel, each module is shifted around its axis by 20-30 ° relative to the module located above, and the annular distributing module collector is made in the form of a toroid, cut at the pipe connecting the collector to the supply line, and the ends of the collector are hermetically closed.
Сущность предлагаемого технического решения поясняется чертежами: на Фиг.1 схематически показана установка, состоящая из семи модулей; на Фиг.2 и Фиг.З показан модуль с восемью реакционными камерами; на Фиг.4 - схема расположения двух соприкасающихся модулей. The essence of the proposed technical solution is illustrated by the drawings: figure 1 schematically shows an installation consisting of seven modules; 2 and FIG. 3 show a module with eight reaction chambers; figure 4 - arrangement of two contacting modules.
Установка содержит расчетное количество соосно установленных модулей 1, каждый из которых сдвинут вокруг оси по отношению к вышележащему модулю на 20-30°. Каждый модуль 1 имеет кольцевой раздаточный коллектор 2 в виде тороида, разрезанный у патрубка 3, подсоединяющего его фланцем 4 к общей подводящей магистрали 5. Свободные концы кольцевого раздаточного коллектора 2 герметично закрыты. Корпус модуля 1 образован стенками двух концентрично установленных цилиндров - внутреннего 6 и наружного 7 и имеет дно 8 и крышку 9. Полость внутреннего цилиндра 6 образует собирающую емкость модуля 1 , а соединенные собирающие емкости нескольких модулей 1 образуют общую собирающую емкость 10. Внутри корпуса модуля 1 установлены трубчатые реакционные камеры 11 с ферромагнитными частицами (не показаны), на каждой из которых закреплен индуктор вращающегося магнитного поля 12. Выходные концы реакционных камер 11 соединены патрубками 13 тангенциально со стенкой внутреннего цилиндра 6. Входные концы реакционных камер 11 соединены с патрубками 14, а те - с кольцевым раздаточным коллектором 2. Модуль 1 снабжен также штуцером 15 для ввода охлаждающего агента и штуцером 16 для его отвода. Для обеспечения кольцевого движения хладагента в каждом модуле 1 между штуцерами 15 и 16 установлена глухая перегородка 17. Установка содержит соединенную с собирающей емкостью 10 дополнительную камеру 18 в виде полого цилиндра, полый конус 19, шламоприемник 20, а также сливной патрубок 21 , отводящую трубу 22, систему фильтров 23, трубопровод для отвода чистого продукта 24, и баки 25 для добавок, 85 подсоединенные к общей подводящей магистрали 5. The installation contains the estimated number of coaxially mounted modules 1, each of which is shifted around the axis with respect to the overlying module by 20-30 °. Each module 1 has an annular distributing manifold 2 in the form of a toroid, cut off at the pipe 3 connecting it with a flange 4 to a common supply line 5. The free ends of the annular distributing collector 2 are hermetically closed. The housing of module 1 is formed by the walls of two concentrically mounted cylinders - the inner 6 and outer 7 and has a bottom 8 and a cover 9. The cavity of the inner cylinder 6 forms a collecting tank of module 1, and the connected collecting tanks of several modules 1 form a common collecting tank 10. Inside the housing of module 1 tubular reaction chambers 11 with ferromagnetic particles (not shown) are installed, on each of which an inductor of a rotating magnetic field 12 is fixed. The output ends of the reaction chambers 11 are connected by tangential nozzles 13 with the wall of the inner cylinder 6. The input ends of the reaction chambers 11 are connected with branch pipes 14, and those - with an annular distributing manifold 2. The module 1 is also provided with fitting 15 for entering the cooling agent and the fitting 16 for its removal. To ensure the circular movement of the refrigerant in each module 1 between the fittings 15 and 16, a blind partition 17 is installed. The installation contains an additional chamber 18 in the form of a hollow cylinder connected to the collecting tank 10, a hollow cone 19, a sludge collector 20, and also a drain pipe 21, a discharge pipe 22 filter system 23, a pipe for the removal of pure product 24, and tanks 25 for additives, 85 connected to a common supply line 5.
Установка работает следующим образом. Включают систему охлаждения индукторов 12, затем питание индукторов 12 и одновременно подачу исходного продукта в реакционные камеры 11 из коллекторов 2. Выполнение коллекторов 2 в виде разомкнутого Installation works as follows. The cooling system of the inductors 12 is turned on, then the inductors 12 are fed and at the same time the initial product is fed into the reaction chambers 11 from the collectors 2. The collectors 2 are made open
90 тороида с герметично закрытыми концами предотвращает вращательное движение потока исходного продукта внутри коллектора 2. Исходный продукт, обработанный в реакционных камерах 11 ферромагнитными частицами, распадается с выделением твердой фазы. Гетерогенная смесь через патрубки 13 попадает в собирающие90 toroids with hermetically sealed ends prevents the rotational movement of the flow of the initial product inside the collector 2. The initial product treated in the reaction chambers 11 with ferromagnetic particles decays with the release of a solid phase. The heterogeneous mixture through nozzles 13 enters the collecting
95 емкости модулей 1 по касательной к стенкам внутренних цилиндров 6. 95 of the capacity of the modules 1 tangentially to the walls of the inner cylinders 6.
Вследствие сдвига одного модуля относительно другого, расположенного выше, происходит дробление потока, а, следовательно, более сильный его разгон. Под воздействием центробежной силы твердые частицы смещаются к стенкам общей Due to the shift of one module relative to the other, located above, there is a fragmentation of the flow, and, therefore, its more powerful acceleration. Under the influence of centrifugal force, solid particles are displaced to the walls of the common
100 собирающей емкости 10, сползают вниз в дополнительную камеру 18 и через конус 19 попадают в шламоприемник 20. Осветленный продукт по сливному патрубку 21 и трубопроводу 22 поступает для дальнейшей очистки от твердых частиц в систему фильтров 23, а чистый продукт идет по трубопроводу 24 к потребителю. 100 of the collecting tank 10, slide down into the additional chamber 18 and through the cone 19 fall into the sludge receptacle 20. The clarified product through the drain pipe 21 and the pipe 22 enters for further purification of solid particles in the filter system 23, and the clean product goes through the pipe 24 to the consumer .
105 Представленная на Фиг.1 установка содержит семь модулей, каждый из которых содержит восемь индукторов, и имеет производительность около 120м3/ч. Каждый модуль работает независимо от других и может содержать до двенадцати реакционных камер с общей производительностью до 250м3/ч. Производительность105 The installation shown in FIG. 1 contains seven modules, each of which contains eight inductors, and has a capacity of about 120 m 3 / h. Each module works independently of the others and can contain up to twelve reaction chambers with a total capacity of up to 250 m 3 / h. Performance
ПО установки может быть увеличена добавкой новых модулей. Так производительность установки при десяти модулях может достигать до 2500 м3/ч. Installation software can be enhanced by adding new modules. So the installation performance with ten modules can reach up to 2500 m 3 / h.
Claims
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/RU2013/000486 WO2014200383A1 (en) | 2013-06-13 | 2013-06-13 | Installation for activating phase separation process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/RU2013/000486 WO2014200383A1 (en) | 2013-06-13 | 2013-06-13 | Installation for activating phase separation process |
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| Publication Number | Publication Date |
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| WO2014200383A1 true WO2014200383A1 (en) | 2014-12-18 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/RU2013/000486 Ceased WO2014200383A1 (en) | 2013-06-13 | 2013-06-13 | Installation for activating phase separation process |
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| Country | Link |
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| WO (1) | WO2014200383A1 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU45306U1 (en) * | 2005-01-13 | 2005-05-10 | Кузьмин Павел Геннадьевич | INSTALLATION FOR ACTIVATION OF PROCESSES AND PHASE SEPARATION |
| RU79055U1 (en) * | 2008-09-11 | 2008-12-20 | Белецкий Валерий Борисович | INSTALLATION FOR ACTIVATION OF THE PHASE SEPARATION PROCESS |
| DE102008047852A1 (en) * | 2008-09-18 | 2010-04-22 | Siemens Aktiengesellschaft | Separating device for separating a mixture of magnetizable and non-magnetizable particles contained in a suspension guided in a separation channel |
-
2013
- 2013-06-13 WO PCT/RU2013/000486 patent/WO2014200383A1/en not_active Ceased
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU45306U1 (en) * | 2005-01-13 | 2005-05-10 | Кузьмин Павел Геннадьевич | INSTALLATION FOR ACTIVATION OF PROCESSES AND PHASE SEPARATION |
| RU79055U1 (en) * | 2008-09-11 | 2008-12-20 | Белецкий Валерий Борисович | INSTALLATION FOR ACTIVATION OF THE PHASE SEPARATION PROCESS |
| DE102008047852A1 (en) * | 2008-09-18 | 2010-04-22 | Siemens Aktiengesellschaft | Separating device for separating a mixture of magnetizable and non-magnetizable particles contained in a suspension guided in a separation channel |
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