• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
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  • 优先权
    • 专利摘要:
    The present invention describes a liquid-liquid extraction column with perforated trays and spillways, presenting a majority of so-called "open" trays and a minority of so-called "closed" trays, the two types of trays differing in the degree of perforation. Application of said column to liquid-liquid system treatment with variable coalescence over time. The application is intended for the extraction of sulfur compounds.
    公开号:CH707268B1
    申请号:CH01917/13
    申请日:2013-11-15
    公开日:2017-10-13
    发明作者:Leinekugel-Le Cocq Damien；Augier Frédéric；Digne Romina；Baudot Arnaud
    申请人:Ifp Energies Now；
    IPC主号:
    专利说明:

    Description
    FIELD OF THE INVENTION [0001] The invention relates to the field of liquid-liquid extraction or solvent extraction operations, bringing a hydrocarbon phase into contact with a phase that is partially immiscible with the hydrocarbon feedstock and containing a fraction of water. . The invention is particularly suitable for the extraction of sulfur compounds from a hydrocarbon phase with an aqueous solution of sodium hydroxide (representing from 10 to 20% by weight), the hydrocarbon phase then being the dispersed phase.
    Examination of the Prior Art [0002] The principle of solvent extraction between two partially immiscible liquid phases has been known for several decades. If a raffinate phase containing the solute is brought into contact with an extracted phase containing no (or little) phase, a transfer of the solute takes place from one phase to the other until a thermodynamic equilibrium is reached between the two phases.
    The phenomenon is greatly facilitated if, at thermodynamic equilibrium, the concentration of solute in the extracted phase is greater than that in the raffinate phase. The concentration ratio between these two phases at equilibrium is called the partition coefficient. A usual implementation of the liquid-liquid extraction consists in bringing the two liquids into contact in countercurrent, ie in opposite flow directions. In case of extraction in a column positioned vertically, it is called a light phase and a heavy phase.
    [0004] A very common case is that of systems composed of an organic or hydrocarbon phase and an aqueous phase. In this case, the aqueous phase is very often the heavy phase. In the liquid-liquid extraction, it is also necessary to distinguish the continuous phase and the dispersed phase.
    The continuous phase follows a flow as close as possible to the piston flow, that is to say without retromé-lange.
    The dispersed phase follows a flow generally against the current of that of the continuous phase and passes through a system of perforated trays that allows the formation of droplets, droplets that coalesce to form a coalesced layer located under each perforated tray when the phase dispersed is the light phase (above each plateau when the dispersed phase is the heavy phase). The exchanges of matter between continuous phase and dispersed phase are essentially between the droplets of the dispersed phase and the continuous phase flowing over each plate.
    The implementation against the current makes it possible to build several successive theoretical stages in the column and thus achieve an extraction efficiency much greater than that obtained with a single stage corresponding to the thermodynamic equilibrium.
    [0008] A more precise description of the liquid-liquid extraction operations is provided in numerous dedicated works, including Handbook of Solvent Extraction of Lo, Baird & Hanson, Krieger Publishing Company, Malabar, 1991, or Transport Phenomena in Liquid Extraction from Laddha & Degaleesan, Tata McGraw-Hill Publishing Co Ltd, 1976.
    The concepts of theoretical stages are described in particular, which is an important point to understand the interest of the invention.
    Many extraction technologies are based on the dispersion of one phase in the other, and it is called disperse phase and continuous phase. The dispersed phase may be the heavy or light phase.
    When the partition coefficient of a solute to be extracted is very high, that is to say that the solute is very easily transferred into the extracted phase, the liquid-liquid extraction columns against the current are operated with a very low extracted phase flow rate relative to the raffinate phase flow rate. As a result, one of the two liquid phases moves in the column at a very low average speed with respect to the other phase. In this case, very particular attention must be paid to the hydrodynamics in the column, because there is a great risk of not operating effectively the column, and not to reach more than one theoretical stage. The benefit of the countercurrent operation may be diminished due to a lower than expected extraction efficiency.
    For example, when the dispersed phase is the phase that has the largest flow, it is possible that the displacement of the droplets causes a little continuous phase in their wakes, which tends to move said continuous phase in the direction opposed to its average movement.
    In the extreme case, the flow of the continuous phase becomes comparable to that of a single perfectly stirred reactor, and the solute concentrations in the continuous phase are homogeneous in the column. The number of theoretical stages of the apparatus is then 1. When the ratio of flow rates between phases extracted (E) and raffinate (R), noted E / R, exceeds 5 or is less than 0.2, a technology Extraction column trays and weirs is often used.
    This technology is based on the division of the column into separate compartments two by two perforated tray equipped with a weir. The function of the plate is to coalesce the dispersed phase on one side of the plate and redisperse the same phase on the other side, through the perforations of the plate.
    This ensures a mono-directional flow of the dispersed phase between a compartment and the next compartment. Similarly, forming a phase coalesced layer initially dispersed on one side of the plate prevents the passage of the continuous phase through the perforations of the plate.
    The number and size of the plate perforations are chosen to generate a pressure drop which will induce the formation of a coalesced layer of dispersed phase having a desired thickness under given operating conditions.
    For example, in case of light dispersed phase, the perforations may be chosen to form a coalesced light phase layer under each tray, a layer typically between 40 mm and 100 mm thick.
    The coalesced layer must be quite thick over the entire section of the column to prevent the passage of the continuous phase through the perforations of the tray. However, a layer that is too thick is detrimental to the extraction efficiency, since this reduces the volume in which the transfer between liquid phases takes place, that is to say the volume in which the dispersed phase droplets are present. .
    The plate of a liquid-liquid extraction column is generally equipped with a weir whose geometry and location are chosen to allow the displacement of the continuous phase from one compartment to another, in the opposite direction to the displacement of the dispersed phase.
    In addition, the geometry of the weir is chosen to limit the entrainment of dispersed phase droplets, such a drive having the effect of degrading the overall performance of the extraction by reducing the number of associated theoretical stages. A criterion of maximum speed in the weir is therefore often imposed not to cause droplets of dispersed phase.
    The successive trays of the extraction column are staggered so that the continuous phase passes through the compartment in its entire width before entering a new weir.
    Spillways D-shaped, more generally arc-shaped, are often used because of their simplicity and the fact that they cover a large fraction of the diameter of the column, thus minimizing dead volumes. The weir rope is conventionally set between 0.3 and 0.8 times the diameter of the column.
    Several problems can be encountered during the design and operation of perforated tray and weir extractions columns.
    If the dispersed phase flow rate is greater than ten times the continuous phase flow, it becomes difficult to design weirs to both prevent the entrainment of droplets, having a rope representing a large fraction of the diameter of column, and sufficiently compartmentalize the flow of the continuous phase to prevent re-mixing thereof in the column.
    It is then sometimes suggested to implement trays having very small sections of weirs, as mentioned in US Patents 4,207,174 and US 6,749,741 B1. To limit droplet entrainment, the compartments are equipped with baffles and internal partitions which limit the area of the compartment in which contact between the liquid phases is possible. As a result, this type of trays offers a small contact surface between phases, which is detrimental to the efficiency of the extraction.
    The interfacial tension of the treated liquid-liquid system is an important parameter because it determines the size of the droplets formed and therefore their terminal velocity. This parameter therefore conditions the maximum speed allowed in the weirs without dispersed phase entrainment, and therefore conditions the minimum section of the weirs.
    Another problem encountered is related to the ease of coalescence of dispersed phase droplets. If the system is very coalescent, a small scattered phase thickness is required to recoalesce the drops and form a continuous layer before crossing the plateau.
    By cons if the coalescence between droplets is slow, it is necessary to ensure a certain contact time between droplets before they coalesce. As a result, the trays are only effective if the dispersed phase layer is important under or on the trays, depending on whether the dispersed phase is light or heavy respectively.
    It is then necessary to reduce the total section of the perforations to increase the pressure drop associated with the traversing trays and thus increase the coalesced phase thickness. This often requires, as a consequence, to increase the distance between trays.
    It is easily understood that, according to the coalescing or little coalescing character of the system, and following its interfacial tension, the optimal plateau will not have the same geometry.
    A plateau defined to treat mainly a very coalescent system and high interfacial tension may have a very degraded operation in case of interfacial tension drop due to the entrainment of droplets in the weirs, or in case of slower coalescence due to continuous phase transition through the trays.
    The present invention describes a liquid-liquid extraction column equipped with trays and weirs, which allows to maintain the extraction performance despite possible changes in interfacial tension, and more or less coalescent character of the system. US 4,081,354 teaches a liquid-liquid extraction process having varying dispersed phase rates. It does not specify any variation in the degree of opening of the trays used.
    US 2,794,711 teaches a device for bringing into intimate contact two liquids by means of contact trays and dispersion baffles. No information on a possible difference in the degree of opening of the trays is provided in this document.
    Brief description of figures [0034]
    Fig. 1 represents an overall view of an extraction column according to the invention in the case of dispersed light phase.
    Fig. 2 represents an overall view of a column according to the invention in case of modification of an existing column initially comprising perforated trays and conventional weirs.
    Fig. 3 shows a detailed view of a closed plate with through weir according to the invention in case of existing column modification.
    Fig. 4 shows a detailed view of the column according to the invention with the addition of a filter medium under the closed tray.
    Fig. 5 represents an overall view of the column according to the invention in case of dispersed heavy phase. Brief description of the invention [0035] The invention relates to a countercurrent liquid-liquid extraction column with perforated trays with weirs requiring a limited number of theoretical stages (2 <NET <4), and within which the partition coefficient of the solute to be extracted is very high so that the extracted phase flow rate is very low compared to the raffinate phase flow rate.
    The partition coefficient is defined as the ratio of the molar concentration of solute in the extract to the molar concentration of solute in the raffinate at equilibrium.
    In the context of the present invention, this partition coefficient is> 50.
    The object of the invention is to ensure proper operation of the extraction column even in case of variations in properties of the treated liquid-liquid system (interfacial tension, coalescing character of the dispersed phase ...).
    The device of the invention combines innovatively two types of perforated trays spillways with distinct geometries and operations.
    The two different types of trays both by the perforation section and the weir section. We thus define in the rest of the text the so-called "open" tray as having a given perforation section and a weir section, and the so-called "closed" tray as having a section of perforations and a weir section that are smaller than those of open tray.
    The invention is based on the use of a majority of open trays in the column, and a small number, or minority, closed trays distributed within the open trays. A closed tray is always between two open trays.
    The number of open trays is between 4 and 25, preferably between 6 and 20, and that of the closed trays is between 1 and 3 and preferably between 1 and 2. The open trays are defined to obtain optimal operation by presence of a coalescent system with high interfacial tension, that is to say having a coalescence time between two drops in contact less than 2 seconds, and an interfacial tension greater than 15 mN / m.
    As a result, the coalesced layer thickness is maintained between 50 mm and 100 mm. The weir of an open tray is chosen so that the speed of the dispersed phase is not greater than a value between 5 mm / s and 60 mm / s. The maximum value not to be exceeded, in the range of 5 to 60 mm / s, depends on the physicochemical properties of the liquid-liquid system, and especially on its surface tension.
    The closed tray has a smaller perforation section than an open tray, the reduction coefficient of the perforation being between 0.2 and 0.8 and preferably between 0.3 and 0.5 times the perforation of an open tray.
    The perforation of an open tray is typically between 2% and 6% referred to the empty section of the column, and preferably between 3% and 5% of the empty section of the column.
    As a result, the dispersed phase layer coalesced under a closed plate has a thickness of between 100 mm and 1000 mm, preferably between 300 mm and 800 mm. The section of the weir of a closed plate is chosen to be between 0.25 and 1 times the section of the weir of the open plates.
    The invention is particularly well suited to the case of a liquid-liquid system whose coalescent character evolves over time. This type of property variation can be related to various phenomena: a change of load, the use of batch pretreatment, etc. More precisely, the invention is particularly applicable to systems with rapid coalescence most of the time, but which from time to time become less coalescing, or even foaming.
    In this case, a device according to the prior art equipped with trays only open type can have severely reduced separation performance due to the poor coalescence of the dispersed phase, and because of the training of the phase continues through the perforations of the tray. As explained in the section devoted to the examination of the prior art, these two phenomena reduce the number of theoretical stages of the device. When the system is little coalescent, the simplest solution that would be thought by the skilled person, would be to implement a device equipped only with trays more closed, generating a longer contact time of the phase to coalesce before passing through the perforated tray. But such a device would then be inefficient when the liquid-liquid system would become at times rapid coalescence.
    Starting from a rapid coalescence system, the invention allows to maintain good performance, even when the system becomes intermittently less coalescing. In the same way, starting from a slow coalescence system, the invention makes it possible to maintain good performances, even when the system becomes intermittently fast coalescing.
    DETAILED DESCRIPTION OF THE INVENTION More specifically, the invention can be defined as a countercurrent liquid-liquid extraction column with perforated perforated trays requiring a limited number of theoretical stages (2 <NET <4), and in which the partition coefficient of the solute to be extracted is greater than or equal to 50.
    Said extraction column is dimensioned for easily coalescent charges most of the time, but also allows the treatment of weakly coalescent charge or charges easily coalescent, but which, intermittently, may become less coalescent, or weakly coalescent. It therefore has a very wide field of application with regard to the coalescent nature of the liquid-liquid system used, and this clearly distinguishes it from the extraction columns of the prior art.
    Said column comprises two types of separate trays; a majority of open trays defined by a degree of perforation p% of between 2% and 6%, and a minority of closed trays defined by a degree of perforation of between 0.2 and 0.8 times, and preferably between 0, 3 and 0.5 times that of open trays. % Perforation is reported to the empty section of the column. Preferably, the degree of perforation of the open trays is between 3% and 5%.
    Each closed tray is located between two open trays, and the minority of trays closed is located in the middle part of the column, that is to say by dividing it into 2 substantially equal portions, numbered 1 and 2 from top to bottom, in the lower portion of portion 1 or the upper portion of portion number 2.
    According to the present invention, the weirs associated with the closed trays have sections between 0.25 and 1 times that of the weirs of the open trays.
    According to another preferred embodiment, the weirs closed trays have a variable section in the sense that they have a first section followed, in the direction of the flow of the liquid, a second section of larger size than the first. .
    According to an equally preferred variant of the present invention, a closed tray occupies the space corresponding to two open trays, and in this case, the weir associated with said closed tray comprises a portion traversing the column substantially in a diameter, so as to the outlet of said weir is opposite to its inlet. According to another variant of the present invention, under certain closed trays is a layer of packing intended to promote coalescence, the thickness of said layer being less than the height of the weir of the closed tray considered.
    According to the present invention, the number of open plates is between 4 and 25, and very preferably, it is between 6 and 20. The number of closed trays is preferably between 1 and 3, and so very preferred between 1 and 2. In general, the extraction column according to the present invention can treat liquid-liquid systems in which the dispersed phase can be either the light phase or the heavy phase.
    The extraction column according to the present invention is particularly applicable to the extraction of sulfur compounds from a hydrocarbon phase by an aqueous soda solution representing from 10% to 20% by weight, the hydrocarbon phase being the dispersed phase. Preferably, the liquid-liquid extraction column according to the present invention applies to systems in which the flow ratio between the extracted phase (E) and the raffinate phase (R) is between 5 and 50 or ( in the exclusive sense) between 0.02 and 0.2.
    The remainder of the detailed description is made based on the figures.
    FIG. 1 describes a liquid-liquid extraction column 1 according to the invention, supplied with a heavy phase by line 2, and in a light phase via line 3.
    The heavy phase which is the continuous phase comes out at the bottom of the column by the pipe 5, and the light phase which is the dispersed phase comes out in the lead through the pipe 4.
    The column is equipped with 7 open type trays and a closed type tray located half of the column. By numbering the trays from 1 to N from top to bottom, the closed tray is p4, and the open trays are trays 1 to 3 and 5 to 8.
    Each open plate is composed of a perforated plate (6) and a weir (7).
    The pressure drop generated during the traversing of the plates induces the presence of a coalesced dispersed phase layer (8) under each plate.
    The closed type plate is composed of a perforated plate (9) and a weir (10). The perforations of the closed tray are defined by a degree of perforation relative to the perforations of an open tray. The degree of perforation of a closed tray is between 0.2 and 0.8 times that of an open tray, and preferably between 0.3 and 0.5 times said perforation of an open tray.
    The cross section and the shape of the weir of the closed plate can be constant over its entire length, or variables as shown in FIG. 1.
    Constant or variable, the section of the weir of a closed tray is between 0.25 and 1 times the section of the spillway of an open tray.
    The coalesced layer (11) generated under the closed tray is then greater than the coalesced layer (8) under the open trays, which may require a spacing between a closed tray and the open tray located below, upper at the spacing between two successive open trays.
    FIG. 2 illustrates the invention in the case of an existing extraction column initially equipped with trays only open type. This case corresponds to the remodeling of an existing column to deal with liquid-liquid systems that can be weakly coalescing at times.
    In this case, the implementation of the invention consists in modifying an open tray by plugging a fraction of the perforations so as to reach the range of 0.2 to 0.8 times the initial perforation, and to remove the lower open tray so as to leave sufficient free space for the coalesced layer (11) of dispersed phase which will become larger following the reduction of the degree of perforation.
    It is then also necessary to modify the weir (10) of the closed tray thus formed to reduce its section in a ratio which is between 0.25 and 1 times the section of the weirs open trays.
    To respect the orientation of the existing open trays, the weir (10) uses bends so as to conduct the liquid phase of the opposite side to that of said weir (10) as shown in FIG. 2. This is called through weir, since the weir (10) has a slightly inclined portion extending substantially over the width of the column. The weir (10) of the closed tray No. 4 communicates with the weir of the open tray located below (plate No. 5) as shown in FIG. 2. The weir (12) of the open tray below the closed tray No. 4 can thus be preserved.
    FIG. 3 shows in greater detail the perforated plate (9) of the upper closed plate, the weir of this plate with a first portion (10) and a second substantially horizontal portion, and the connection of the weir with the open plate located below (plateau lower) by means of a third vertical portion (12) with a section greater than that of the section of the first portion (10).
    FIG. 3 also shows that the thickness of the coalesced layer (11) under the upper closed plate is greater than the thickness of the coalesced layer (8) under the open plate located below (lower plate).
    FIG. 4 illustrates a particular implementation of the invention. To facilitate coalescence between the droplets, a porous filter medium (13) is introduced under the closed plate (9), which improves the performance of the invention in case of very low coalescing system. The spillway (10) then passes through the porous medium (13) and is expanded in an end portion (12) to feed the lower open plate (6).
    The coalesced layer is normally below the plate (9), and the interface (11) between this coalesced layer and the liquid phase with dispersed drops may be below the lining (13).
    FIG. Illustrates the invention in the case where the heavy phase is the dispersed phase.
    The light phase is introduced through the lower pipe (2) and out through the upper pipe (5).
    The heavy phase is introduced through the upper pipe (3) and out through the lower pipe (4).
    The coalesced layer (8) is located above each open plate such as (6).
    权利要求:
    Claims (9)
    [1]
    The coalesced layer (11) is also above the closed plate (9), but is larger than the coalesced layer corresponding to an open plate. The operation of the extraction column according to the invention is the same as in the case where the dispersed phase is the light phase. The two technological differences with respect to the case of the light dispersed phase are: - Weirs (10), (12) are then oriented upwards. - The optional coalescing media (13) is positioned above the closed tray. Comparative Example [0084] The following comparative example is obtained by simulation. The feedstock to be treated is a hydrocarbon containing 100 ppm methanethiol. The solvent used to extract methanethiol is a 20% sodium hydroxide solution. The dispersed phase is the hydrocarbon phase. The flow rates of hydrocarbon and sodium hydroxide are 150 and 10 m3 / h respectively. The extraction is carried out at 30 ° C. and under 10 bars absolute. Three separate devices are used to perform the extraction. The device 1 said "open trays" is according to the prior art. It consists of an extraction column equipped with 15 perforated trays with weirs, 1 m apart and 3 m in diameter. The perforations are 5mm in diameter and the perforated surface is equal to 3% of the column section. The weirs have an area equal to 20% of the column section. The device 2, still according to the prior art, is called "closed trays". It is in all respects similar to the device 1, but the perforated surface is equal to 1% of the column section, the weir surface is equal to 10% of the column section. The device 3 is according to the invention. It consists of an extraction column equipped with 14 open-type trays, such as those equipping the device 1, and 1 closed-type tray such as those equipping the device 2. [0093] The closed tray is positioned at mid-column height, that is to say positioned above 7 first open trays and below 7 other open trays. When the liquid-liquid system has a rapid coalescence, set at 2s, the efficiency of an open type plate is 20% compared to a theoretical stage, that of a closed plate is 10%. When the liquid-liquid system has a slow coalescence, considered here at 20 seconds, the effectiveness of a closed tray is always 10%, against that of an open tray is strongly modified. Indeed the open trays then no longer allow to ensure a flow against the current because the heavy phase undergoes a very strong back-mixing through the trays. As a result, a series of successive open trays of at least 5 trays then behaves as a single theoretical stage. The presence of a carefully closed type closed tray allows to compartmentalize the flow of the heavy phase. The equivalent number of theoretical stages resulting from the 3 devices, depending on the system in question is given in Table 1 below: Device 1 Device 2 Device 3 Coalescing system 2.8 1.4 2.68 Coalescent system Table 1: Number of equivalent theoretical stages for the devices 1 to 3 The interest of the invention appears clearly on reading Table 1. The performances of the column according to the invention (device 3) are almost identical to that of the open tray column (device 1) in case of coalescing system, and much higher than the other two columns (devices 1 and 2) in the case of a coalescent system. claims
    1. Countercurrent liquid-liquid extraction column with perforated weir trays having a limited number of theoretical stages between 2 and 4, and in which the partition coefficient of the solute to be extracted is greater than or equal to 50, the liquid-liquid system may have a coalescence variable in time, said column having two types of separate trays; a number of open trays of between 4 and 25, defined by a degree of perforation p% of between 2% and 6%, and a number of closed trays of between 1 and 3, the column being characterized by: each closed tray is defined by a degree of perforation between 0.3 and 0.5 times that of the open trays, - each closed tray is located between two open trays, and - the closed trays are located in the middle part of the column, it is to say by dividing it into 2 substantially equal portions, numbered 1 and 2 from top to bottom, in the lower portion of the portion 1 or the upper portion of the portion number 2, - weirs associated with closed trays have sections between 0.25 and 1 times the weirs of open trays.
    [2]
    2. liquid-liquid extraction column according to claim 1, wherein a closed tray occupies the space corresponding to two open trays, and in this case, the weir associated with said closed tray has a portion passing through the column so that that the outlet of said weir is opposite to its entrance.
    [3]
    3. liquid-liquid extraction column according to claim 1, wherein under certain closed trays is a layer of packing intended to promote coalescence, the thickness of said packing layer being less than the height of the chute of the closed tray considered.
    [4]
    4. liquid-liquid extraction column according to claim 1, wherein the number of open trays is between 6 and 20, and the number of trays closed is between 1 and 2.
    [5]
    5. Use of the extraction column according to one of claims 1 to 4, for an extraction of sulfur compounds of a hydrocarbon phase with an aqueous sodium hydroxide solution representing 10 to 20% by weight, the hydrocarbon phase being the dispersed phase.
    [6]
    6. Use of the extraction column according to one of claims 1 to 4, in an extraction process in which the flow ratio between the extracted phase (E) and the raffinate phase (R) is between 5 and 50.
    [7]
    7. Use of the extraction column according to one of claims 1 to 4, in an extraction process in which the flow ratio between the extracted phase (E) and the raffinate phase (R) is between 0, 02 and 0.2.
    [8]
    8. Use of the extraction column according to one of claims 1 to 4, in an extraction process in which the dispersed phase is the light phase.
    [9]
    9. Use of the extraction column according to one of claims 1 to 4, in an extraction process in which the dispersed phase is the heavy phase.
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    同族专利:
    公开号 | 公开日
    US9333442B2|2016-05-10|
    FR2998190B1|2015-10-16|
    KR102165628B1|2020-10-14|
    FR2998190A1|2014-05-23|
    US20140142342A1|2014-05-22|
    KR20140064669A|2014-05-28|
    CH707268A2|2014-05-30|
    引用文献:
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    法律状态:
    2018-02-28| PCAR| Change of the address of the representative|Free format text: NEW ADDRESS: AVENUE DES MORGINES 12, 1213 PETIT-LANCY (CH) |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1203120A|FR2998190B1|2012-11-20|2012-11-20|LIQUID LIQUID EXTRACTION COLUMN COMPRISING TWO TYPES OF SEPARATE TRAYS|
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