WO2007133120A2 - Device for continuously separating two fluids having different densities - Google Patents
Device for continuously separating two fluids having different densities Download PDFInfo
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- WO2007133120A2 WO2007133120A2 PCT/RU2007/000235 RU2007000235W WO2007133120A2 WO 2007133120 A2 WO2007133120 A2 WO 2007133120A2 RU 2007000235 W RU2007000235 W RU 2007000235W WO 2007133120 A2 WO2007133120 A2 WO 2007133120A2
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- WIPO (PCT)
- Prior art keywords
- partitions
- tank
- lid
- different densities
- baffles
- Prior art date
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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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/24—Pneumatic
- B03D1/26—Air lift machines
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0208—Separation of non-miscible liquids by sedimentation
-
- 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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1406—Flotation machines with special arrangement of a plurality of flotation cells, e.g. positioning a flotation cell inside another
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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
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/14—Flotation machines
- B03D1/1412—Flotation machines with baffles, e.g. at the wall for redirecting settling solids
Definitions
- the proposed solution relates to devices for separating a mixture of liquids of different densities, mainly water with petroleum products, and can be used in the oil refining and petrochemical industries, as well as in the separation of water-oil emulsions, degreasing solutions in painting and galvanic production.
- a known installation for wastewater treatment from oil products and mechanical impurities containing a sump with partitions, a compartment for accumulating oil product, pipes for supplying wastewater, drainage of purified water and oil products, regulators of the levels of oil product and water, the upper edges of the partitions are located at the same level, while the last partition is made blind from below and forms a compartment for purified water, and the purified oil compartment is formed by the last blind partition from below, a pipe for supplying wastewater is located open ytym end upward at the lower edges of the first baffle, and an outlet for removing purified water is situated in the lower part of the settler before the last partition and connected to the water seal and provided with a spray. (see RF patent Ns 2118197 according to class B 01D17 / 028 for 1998)
- a device for the continuous separation of two liquids of different densities including a reservoir, with a drain compartment, tanks connected in series with vertical separation walls installed in them, level tubes, height-adjustable and brought out from the bottom of the tanks into the drain compartment, a liquid heating system in reservoir, while the device is additionally equipped with overflow pockets with a vertical side slot mounted on vertical partitions, drain lot s located above the pockets and partitions themselves are mounted for vertical movement and biased by the top of the tank (see. Author's Certificate USSR tml. The 01 per 1983 D 17/02).
- the disadvantage of this type of device is the design complexity due to the introduction of level tubes and a drain compartment, unreliable and inefficient separation of liquids during operation. This is because with an increase in the supply of the mixture to the first container, its speed increases, and the path length remains constant. As a result, the residence time of the mixture in containers along the surface of the vertical dividing wall decreases, does not have time to effectively separate into fractions and flows into the following containers. In addition, the partitions do not have tightness from below and from the sides, which allows the mixture to flow freely into the cavity of the tank behind the partition.
- the technical result of the proposed device is simplified design, improved quality and increased productivity when cleaning liquids with different densities.
- the specified technical result is achieved by the fact that in the proposed device for the continuous separation of two liquids with different densities, including a tank with a lid, a supply line and drain pipes connected to it, located on opposite sides of the tank, lower vertical solid partitions fixed to the bottom of the tank and drain trays for overflowing the upper layer of liquid beyond the partitions, according to a utility model, the lid of the tank is removable, on the inner surface of which is fixed There are upper solid partitions connected to drain trays, between each pair of lower and upper reservoir partitions there is a gas line with nozzles, the end of which is located in the area between the ends of these partitions, and between each two adjacent lower partitions there is a liquid level indicator with a lower density.
- FIG. 1 - shows a diagram of the proposed device.
- Figure 2 General view of the device with pointers with a local neckline.
- FIG. 3 is a section along A-A of FIG. one
- the proposed device comprises a tank 1, inside which vertical lower partitions 4 and 5 are rigidly and hermetically attached to its bottom 2 and its sides 3. Partitions 4 and 5 simultaneously divide the entire internal cavity of the tank 1 into several containers 6, and the depth of the containers decreases from the side wall 7 towards the side wall 8 of the tank 1.
- the tank 1 On the wall 7, mainly above the largest of the partitions 5, the tank 1 is equipped with a supply line 9 for a mixture of liquids 10.
- On top of the tank 1 is closed by a removable cover 11 on which the upper partitions 12 and 13 are fixed. Drain trays 14 are attached to the partitions 12 and the other end is connected with partitions 13.
- the partitions 13 above the trays 14 are provided with through channels 15.
- Each of the containers 6 of the tank 1 is equipped with an air line 16 located between the lower partitions 4 and the upper partitions 13. At the free end, the line 16 nabzhena injectors 17, the output of which is located below the end 18 above the baffles 5 and the end walls 19, 13.
- the liquid level gauges 22 In each of the tanks 6 between the upper partition wall 12 in the cover 11 through holes 20 and 21 set the liquid level gauges 22 with a lower density.
- On the side wall 8 of the tank 1 there are openings 24 and 23 for removing separately from the last tank 6 separately liquid 22 with lower density and liquid 25 with higher density.
- the mixture of liquids 10 is fed into the tank 1 through the supply line 9 and fills the first of the containers 6 to the level of the lower partition 5, and then pours through its end 18 into the next of the containers 6 and so on to the end of the tank.
- the mixture 9 takes on a static state and the mixture is divided into the light fraction 22 and the heavy fraction 25.
- the light fraction emerges on the surface of the heavy fraction and accumulates and is retained by the upper partitions 12.
- the heavy fraction 25 of the mixture 9 together with the remaining part of the light fraction 22 is poured into following from capacities 6 and from the last already completely cleaned is removed through the hole 24 from the tank 1. This process is carried out continuously and in automatic mode.
- the light fraction 22 of the mixture 9 can be removed from the tank 1 in two ways.
- the separated fraction 22 through the openings 15 of the upper partitions 12 flows from the containers 6 and is discharged from the reservoir 1 through the opening 23.
- the second method for removing the light fraction 22 is as follows. In the upper partitions 12 there are through holes 20, and on the dividing line of the fractions there is a float 21, to which a pump is connected. Moving in a vertical plane, the float 21 automatically evacuates the light fraction 22 from all containers 6 alternately or simultaneously. The solids in the mixture 9 settle on the bottom 2 of the tank and are removed from it by one of the known methods, for example, mechanically. The presence of the air line 16 causes the light fraction to tear into pieces and raise it above the level of the heavy fraction 25, which connects to the already separated light fraction 22 and does not mix with the upper layer of the heavy fraction 25.
- the proposed device when separating mixtures into fractions allows a more intensive process of separating the mixture, regardless of the amount of the mixture.
- the device itself is simpler to manufacture and more mobile in comparison with the known designs of devices of a similar purpose.
- Another advantage of the proposed device is that the movement of liquids inside the tank is carried out without additional devices, which makes it economical in the process operation.
- the presence of a removable cover allows you to visually monitor the process, monitor the health of all nodes and completely eliminate the ingress of foreign objects into the device, both during operation and in non-working condition.
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- Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Extraction Or Liquid Replacement (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention relates to devices for separating mixtures of fluids having different densities, mainly for separating water and petroleum products, and can be used in the petroleum-refining and petrochemical industries and in painting and galvanic process for separating water-oil emulsions and degreasing solutions. The inventive device makes it possible to simplify the structural design, to improve the quality and to increase the performance of cleaning of fluids having different densities. The device for continuously separating two fluids having different densities comprises a container provided with a lid and a supplying line and drain pipes which are connected thereto and disposed on the opposite sides thereof, lower vertical continuous baffles fixed to the container bottom and overflow launders for evacuating the top layer of a fluid outside the baffles. The lid of the container is embodied in such a way that it is removable and is provided with top continuous baffles which are fixed to the internal surface thereof and are connected to said overflow launders, a gas line, which is provided with nozzles and whose end surface is arranged between the end surfaces of the container top and lower baffles, is places therebetween and a lever meter for the fluid having a smaller density is mounted between each adjacent pair of the lower baffles.
Description
Устройство для непрерывного разделения двух жидкостей различной плотности Device for the continuous separation of two liquids of different densities
Предлагаемое техническое решение относится к устройствам для разделения смеси жидкостей с различной плотностью, преимущественно воды с нефтепродуктами, и может быть использовано в нефтеперерабатывающей и нефтехимической промышленности, а так же при разделении водно-масляных эмульсий, обезжиривающих растворов в окрасочном и гальваническом производстве.The proposed solution relates to devices for separating a mixture of liquids of different densities, mainly water with petroleum products, and can be used in the oil refining and petrochemical industries, as well as in the separation of water-oil emulsions, degreasing solutions in painting and galvanic production.
Известна установка для очистки сточных вод от нефтепродуктов и механических примесей , содержащая отстойник с перегородками, отсек для накопления нефтепродукта, патрубки для подачи сточной воды, отвода очищенной воды и нефтепродуктов, регуляторы уровней нефтепродукта и воды, верхние кромки перегородок расположены на одном уровне, при этом последняя перегородка выполнена глухой снизу и образует отсек для очищенной воды, а отсек очищенной нефти образован последней глухой перегородкой снизу, патрубок для подачи сточной воды размещен открытым концом вверх на уровне нижней кромки первой перегородки, а патрубок для отвода очищенной воды расположен в нижней части отстойника перед последней перегородкой и соединен с гидрозатвором и снабжен распылителем. ( см. патент РФ Ns 2118197 по кл. В 01D17/028 за 1998 г.)A known installation for wastewater treatment from oil products and mechanical impurities, containing a sump with partitions, a compartment for accumulating oil product, pipes for supplying wastewater, drainage of purified water and oil products, regulators of the levels of oil product and water, the upper edges of the partitions are located at the same level, while the last partition is made blind from below and forms a compartment for purified water, and the purified oil compartment is formed by the last blind partition from below, a pipe for supplying wastewater is located open ytym end upward at the lower edges of the first baffle, and an outlet for removing purified water is situated in the lower part of the settler before the last partition and connected to the water seal and provided with a spray. (see RF patent Ns 2118197 according to class B 01D17 / 028 for 1998)
Недостатком данных установок является грубое качество очистки воды от нефтепродуктов из-за перемешивания компонентов при переливе их в соответствующие резервуары, потому что идет постоянное движение в верхней части жидкостей и поэтому вода находится постоянно в слое нефтепродуктов, а сами нефтепродукты
присутствуют в верхнем слое воды. Кроме того, установка потребляет много энергии на подачу воды на распыление и снижает производительность самой установке в процессе очистки.The disadvantage of these installations is the rough quality of water purification from oil products due to mixing of the components when they are poured into appropriate tanks, because there is constant movement in the upper part of the liquids and therefore water is constantly in the layer of oil products, and the oil products themselves present in the upper layer of water. In addition, the installation consumes a lot of energy for spraying water and reduces the productivity of the installation itself during the cleaning process.
Известно устройство для непрерывного разделения двух жидкостей различной плотности, включающее резервуар, со сливным отсеком, последовательно соединенные между собой емкости с установленными в них вертикальными разделительными перегородками, уровневые трубки, регулируемые по высоте и выведенные из нижней части емкостей в сливной отсек , систему подогрева жидкости в резервуаре, при этом устройство дополнительно снабжено переливными карманами с вертикальной боковой прорезью, установленными на вертикальных перегородках, сливными лотками расположенными над карманами , а сами перегородки установлены с возможностью вертикального перемещения и подпружинены со стороны верхней части резервуара ( см. Авторское свидетельство СССР по кл. В 01 D 17/02 за 1983г.)A device for the continuous separation of two liquids of different densities, including a reservoir, with a drain compartment, tanks connected in series with vertical separation walls installed in them, level tubes, height-adjustable and brought out from the bottom of the tanks into the drain compartment, a liquid heating system in reservoir, while the device is additionally equipped with overflow pockets with a vertical side slot mounted on vertical partitions, drain lot s located above the pockets and partitions themselves are mounted for vertical movement and biased by the top of the tank (see. Author's Certificate USSR tml. The 01 per 1983 D 17/02).
Недостатком данного вида устройств является сложность конструкции из-за введения уровневых трубок и сливного отсека, ненадежное и неэффективное разделение жидкостей в процессе эксплуатации. Это происходит потому, что при увеличении подачи смеси в первую емкость, скорость ее увеличивается, а длина пути остается постоянной. В результате уменьшается время нахождения смеси в емкостях вдоль поверхности вертикальной разделительной перегородки, не успевает эффективно разделиться по фракциям и перетекает в следующие емкости. Кроме того, перегородки не имеют герметичности снизу и с боков, что позволяет смеси свободно перетекать в полость емкости за перегородкой.The disadvantage of this type of device is the design complexity due to the introduction of level tubes and a drain compartment, unreliable and inefficient separation of liquids during operation. This is because with an increase in the supply of the mixture to the first container, its speed increases, and the path length remains constant. As a result, the residence time of the mixture in containers along the surface of the vertical dividing wall decreases, does not have time to effectively separate into fractions and flows into the following containers. In addition, the partitions do not have tightness from below and from the sides, which allows the mixture to flow freely into the cavity of the tank behind the partition.
Техническим результатом предлагаемого устройства является
упрощение конструкции, улучшения качества и повышении производительности при очистки жидкостей с различной плотностью.The technical result of the proposed device is simplified design, improved quality and increased productivity when cleaning liquids with different densities.
Указанный технический результат достигается тем, что в предлагаемом устройстве для непрерывного разделения двух жидкостей с различной плотностью, включающем резервуар с крышкой, соединенные с ним подающую магистраль и сливные патрубки, расположенные на противоположных сторонах резервуара, нижние вертикальные сплошные перегородки, закрепленные на дне резервуара и сливные лотки для перелива верхнего слоя жидкости за перегородки, согласно полезной модели, крышка резервуара выполнена съемной, на внутренней поверхности которой закреплены верхние сплошные перегородки, соединенные со сливными лотками, между каждой парой нижней и верхней перегородок резервуара расположена газовая магистраль с форсунками, торец которой расположен в зоне между торцами этих перегородок, а между каждыми двумя смежными нижними перегородками имеется указатель уровня жидкости с меньшей плотностью.The specified technical result is achieved by the fact that in the proposed device for the continuous separation of two liquids with different densities, including a tank with a lid, a supply line and drain pipes connected to it, located on opposite sides of the tank, lower vertical solid partitions fixed to the bottom of the tank and drain trays for overflowing the upper layer of liquid beyond the partitions, according to a utility model, the lid of the tank is removable, on the inner surface of which is fixed There are upper solid partitions connected to drain trays, between each pair of lower and upper reservoir partitions there is a gas line with nozzles, the end of which is located in the area between the ends of these partitions, and between each two adjacent lower partitions there is a liquid level indicator with a lower density.
На фиг. 1 - изображена схема предлагаемого устройства. На фиг.2 - общий вид устройства с указателями с местным вырезом.In FIG. 1 - shows a diagram of the proposed device. Figure 2 - General view of the device with pointers with a local neckline.
На фиг. 3 - изображено сечение по A-A фиг. 1In FIG. 3 is a section along A-A of FIG. one
Предлагаемое устройство содержит резервуар 1, внутри которого к его дну 2 и боковым сторонам 3 жестко и герметично прикреплены вертикальные нижние перегородки 4 и 5. Перегородки 4 и 5 одновременно разделяют всю внутреннюю полость резервуара 1 на несколько емкостей 6, причем глубина емкостей уменьшается от боковой стенки 7 в сторону боковой стенки 8 резервуара 1. На стенке 7,
преимущественно выше самой большой из перегородок 5 резервуар 1 снабжен подающей магистралью 9 для смеси жидкостей 10. Сверху резервуар 1 закрыт съемной крышкой 11, на которой закреплены верхние перегородки 12 и 13. К перегородкам 12 одним из торцев прикреплены сливные лотки 14, а другим торцем соединены с перегородками 13. Перегородки 13 выше лотков 14 снабжены сквозными каналами 15. Каждая из емкостей 6 резервуара 1 снабжена воздушной магистралью 16, размещенной между нижними перегородками 4 и верхними перегородками 13. На свободном конце магистраль 16 снабжена форсунками 17, выход которых расположен ниже торца 18 перегородок 5 и выше торца 19 перегородки 13. В каждой из емкостей 6 между верхними перегородками 12 в крышке 11 выполнены сквозные отверстия 20 и установлены измерители 21 уровня жидкости 22 с меньшей плотностью . На боковой стенке 8 резервуара 1 имеются отверстия 24 и 23 для удаления из последней емкости 6 раздельно жидкости 22 с меньшей плотностью и жидкости 25 с большей плотностью.The proposed device comprises a tank 1, inside which vertical lower partitions 4 and 5 are rigidly and hermetically attached to its bottom 2 and its sides 3. Partitions 4 and 5 simultaneously divide the entire internal cavity of the tank 1 into several containers 6, and the depth of the containers decreases from the side wall 7 towards the side wall 8 of the tank 1. On the wall 7, mainly above the largest of the partitions 5, the tank 1 is equipped with a supply line 9 for a mixture of liquids 10. On top of the tank 1 is closed by a removable cover 11 on which the upper partitions 12 and 13 are fixed. Drain trays 14 are attached to the partitions 12 and the other end is connected with partitions 13. The partitions 13 above the trays 14 are provided with through channels 15. Each of the containers 6 of the tank 1 is equipped with an air line 16 located between the lower partitions 4 and the upper partitions 13. At the free end, the line 16 nabzhena injectors 17, the output of which is located below the end 18 above the baffles 5 and the end walls 19, 13. In each of the tanks 6 between the upper partition wall 12 in the cover 11 through holes 20 and 21 set the liquid level gauges 22 with a lower density. On the side wall 8 of the tank 1 there are openings 24 and 23 for removing separately from the last tank 6 separately liquid 22 with lower density and liquid 25 with higher density.
Смесь жидкостей 10 подается внутрь резервуара 1 через подающую магистраль 9 и заполняет первую из емкостей 6 до уровня нижней перегородки 5, а затем переливается через ее торец 18 в следующую из емкостей 6 и так до конца резервуара. После заполнения емкости 6 смесь 9 принимает статическое состояние и происходит разделение смеси на легкую фракцию 22 и тяжелую фракцию 25. Легкая фракция всплывает на поверхности тяжелой фракции накапливается и удерживается верхними перегородками 12. Тяжелая фракция 25 смеси 9 вместе с оставшейся частью легкой фракции 22 переливается в следующую из емкостей 6 и из последней уже полностью
очищенная удаляется через отверстие 24 из резервуара 1. Этот процесс осуществляется непрерывно и в автоматическом режиме. Легкая же фракция 22 смеси 9 может удаляться из резервуара 1 двумя способами. В первом способе отделенная фракция 22 через отверстия 15 верхних перегородок 12 перетекает из емкостей 6 и выводится из резервуара 1 через отверстие 23. Второй способ удаления легкой фракции 22 заключается в следующем. В верхних перегородках 12 имеются сквозные отверстия 20, а на линии раздела фракций расположен поплавок 21, с которым соединен откачивающий насос. Перемещаясь в вертикальной плоскости поплавок 21 автоматически производит откачку легкой фракции 22 из всех емкостей 6 поочередно или же одновременно. Твердые включения в смеси 9 оседают на дне 2 резервуара и удаляются из него одним из известных способов, например, механически. Наличие воздушной магистрали 16 заставляет легкую фракцию разрывать на части и поднимать ее выше уровня тяжелой фракции 25, которая соединяется с уже отделенной легкой фракцией 22 и не перемешивается с верхним слоем тяжелой фракции 25.The mixture of liquids 10 is fed into the tank 1 through the supply line 9 and fills the first of the containers 6 to the level of the lower partition 5, and then pours through its end 18 into the next of the containers 6 and so on to the end of the tank. After filling the container 6, the mixture 9 takes on a static state and the mixture is divided into the light fraction 22 and the heavy fraction 25. The light fraction emerges on the surface of the heavy fraction and accumulates and is retained by the upper partitions 12. The heavy fraction 25 of the mixture 9 together with the remaining part of the light fraction 22 is poured into following from capacities 6 and from the last already completely cleaned is removed through the hole 24 from the tank 1. This process is carried out continuously and in automatic mode. The light fraction 22 of the mixture 9 can be removed from the tank 1 in two ways. In the first method, the separated fraction 22 through the openings 15 of the upper partitions 12 flows from the containers 6 and is discharged from the reservoir 1 through the opening 23. The second method for removing the light fraction 22 is as follows. In the upper partitions 12 there are through holes 20, and on the dividing line of the fractions there is a float 21, to which a pump is connected. Moving in a vertical plane, the float 21 automatically evacuates the light fraction 22 from all containers 6 alternately or simultaneously. The solids in the mixture 9 settle on the bottom 2 of the tank and are removed from it by one of the known methods, for example, mechanically. The presence of the air line 16 causes the light fraction to tear into pieces and raise it above the level of the heavy fraction 25, which connects to the already separated light fraction 22 and does not mix with the upper layer of the heavy fraction 25.
Использование предлагаемого устройства при разделении смесей по фракциям позволяет более интенсивно производить процесс разделения смеси независимо от количества смеси. Кроме того, само устройство более просто в изготовлении и более мобильно по сравнении с известными конструкциями устройств аналогичного назначения.Using the proposed device when separating mixtures into fractions allows a more intensive process of separating the mixture, regardless of the amount of the mixture. In addition, the device itself is simpler to manufacture and more mobile in comparison with the known designs of devices of a similar purpose.
Еще одним из преимуществ предлагаемого устройства является то, что движение жидкостей внутри резервуара осуществляется без дополнительных устройств, что делает его экономичным в процессе
эксплуатации. Наличие съемной крышки позволяет вести визуальный контроль за процессом, контролировать исправность всех узлов и полностью исключить попадание посторонних предметов внутрь устройства, как в процессе работы, так и в не рабочем состоянии.
Another advantage of the proposed device is that the movement of liquids inside the tank is carried out without additional devices, which makes it economical in the process operation. The presence of a removable cover allows you to visually monitor the process, monitor the health of all nodes and completely eliminate the ingress of foreign objects into the device, both during operation and in non-working condition.
Claims
1. Устройство для непрерывного разделения двух жидкостей различной плотности, включающее резервуар с крышкой, соединенные с ним подающую магистраль и сливные патрубки, расположенные на противоположных сторонах резервуара, нижние вертикальные сплошные перегородки, закрепленные на дне резервуара и сливные лотки для перелива верхнего слоя жидкости за перегородки, отличающееся тем, что крышка резервуара выполнена съемной, на внутренней поверхности которой закреплены верхние сплошные перегородки, соединенные со сливными лотками, между каждой парой нижней и верхней перегородок резервуара расположена газовая магистраль с форсунками, торец которой расположен в зоне между торцами этих перегородок, а между каждыми двумя смежными нижними перегородками имеется указатель уровня жидкости с меньшей плотностью.1. Device for the continuous separation of two liquids of different densities, including a tank with a lid, a supply line and drain pipes connected to it, located on opposite sides of the tank, lower vertical solid partitions fixed to the bottom of the tank and drain trays for overflowing the upper layer of liquid for the partitions characterized in that the lid of the tank is removable, on the inner surface of which are fixed upper solid partitions connected to drain trays, between Each pair of the lower and upper partitions of the reservoir contains a gas line with nozzles, the end of which is located in the zone between the ends of these partitions, and a liquid level indicator with a lower density is located between each two adjacent lower lower partitions.
2. Устройство по п.l, отличающееся тем, что крышка резервуара выполнена наклонной, с вершиной со стороны сливных патрубков.2. The device according to p. 1, characterized in that the lid of the tank is made inclined, with the apex from the side of the drain pipes.
3. Устройство по п.l, отличающееся тем, что длина перегородок на дне резервуара выполнена различной.3. The device according to claim 1, characterized in that the length of the partitions at the bottom of the tank is different.
4. Устройство по п.l, отличающееся тем, что перегородки на крышке резервуара снабжены сквозным каналом, расположенным над сливными лотками.4. The device according to claim 1, characterized in that the partitions on the lid of the tank are provided with a through channel located above the drain trays.
5. Устройство по п.l, отличающееся тем, что торец нижней перегородки расположен выше по уровню по отношению к смежной верхней перегородке. 5. The device according to p. 1, characterized in that the end of the lower partition is located higher in level with respect to the adjacent upper partition.
6. Устройство по п. I3 отличающееся тем, что между каждыми верхними и нижними перегородками в резервуаре выполнена полость для сбора и накапливания определенного количества нефтепродуктов.6. The device according to p. I 3 characterized in that between each of the upper and lower partitions in the tank there is a cavity for collecting and accumulating a certain amount of oil products.
7. Устройство по п.l, отличающееся тем, что указатель уровня выполнен в виде поплавка, тело которого плавает в жидкости с большей плотностью и тонет в жидкости с меньшей плотностью.7. The device according to p. 1, characterized in that the level indicator is made in the form of a float, the body of which floats in a liquid with a higher density and sinks in a liquid with a lower density.
8. Устройство по п.l, отличающееся тем, что в крышке резервуара выполнено одно или несколько сквозных отверстий.8. The device according to claim 1, characterized in that one or more through holes are made in the lid of the tank.
9. Устройство по. п.l, отличающееся тем, что верхние перегородки на крышке имеют П-образную форму в поперечном сечении.9. The device according to. p.l, characterized in that the upper partitions on the lid are U-shaped in cross section.
10. Устройство по п.4, отличающееся тем, что сквозной канал выполнен в виде щели, параллельной сливному лотку. 10. The device according to claim 4, characterized in that the through channel is made in the form of a slit parallel to the drain tray.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2006116762 | 2006-05-15 | ||
| RU2006116762 | 2006-05-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2007133120A2 true WO2007133120A2 (en) | 2007-11-22 |
| WO2007133120A3 WO2007133120A3 (en) | 2008-05-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/RU2007/000235 WO2007133120A2 (en) | 2006-05-15 | 2007-05-14 | Device for continuously separating two fluids having different densities |
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| Country | Link |
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| WO (1) | WO2007133120A2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102784494A (en) * | 2012-06-30 | 2012-11-21 | 惠州市长润发涂料有限公司 | Water separator |
| CN111359305A (en) * | 2020-04-21 | 2020-07-03 | 江苏更美科技有限公司 | Preparation method and device of hyaluronic acid with moisturizing effect for skin care |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105170340B (en) * | 2015-10-12 | 2017-12-15 | 湖南有色金属研究院 | A kind of gas-charging compound cylinders combination type floating optional equipment |
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| SU1386223A1 (en) * | 1985-04-11 | 1988-04-07 | Предприятие П/Я А-7155 | Apparatus for breaking concentrated emulsions "cascade" |
| SU1687577A1 (en) * | 1989-01-12 | 1991-10-30 | Инженерный центр "Трубопровод" | Apparatus for purifying vapour, gas and petroleum containing effluents |
| US5132010A (en) * | 1988-12-07 | 1992-07-21 | Wilhelm Ossenkop | In-line oil-separating equipment with meandering flow |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU1386223A1 (en) * | 1985-04-11 | 1988-04-07 | Предприятие П/Я А-7155 | Apparatus for breaking concentrated emulsions "cascade" |
| US5132010A (en) * | 1988-12-07 | 1992-07-21 | Wilhelm Ossenkop | In-line oil-separating equipment with meandering flow |
| SU1687577A1 (en) * | 1989-01-12 | 1991-10-30 | Инженерный центр "Трубопровод" | Apparatus for purifying vapour, gas and petroleum containing effluents |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102784494A (en) * | 2012-06-30 | 2012-11-21 | 惠州市长润发涂料有限公司 | Water separator |
| CN111359305A (en) * | 2020-04-21 | 2020-07-03 | 江苏更美科技有限公司 | Preparation method and device of hyaluronic acid with moisturizing effect for skin care |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2007133120A3 (en) | 2008-05-02 |
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