• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to a method for producing a composition for use as a filler for a step of producing carbon black from an atmospheric residue, wherein said atmospheric residue is distilled under vacuum to yield at least one vacuum distillate fraction and at least one vacuum residue fraction, said vacuum distillate fraction being treated according to at least the following two successive stages: a fluidized catalytic cracking step 1) leading to an FCC residue, a step 2) for filtering the fine solid particles contained in said FCC residue obtained in step 1) of cracking, resulting in a filtrate containing less than 300 ppm of particles less than 10 microns, and wherein said fraction vacuum residue feeds a deasphalting step leading to a deasphalted vacuum residue fraction of which at least a portion is mixed with at least a portion of said filtrate obtained in the filtration step 2) to form said composition.
    公开号:FR3044319A1
    申请号:FR1561558
    申请日:2015-11-30
    公开日:2017-06-02
    发明作者:Pascal Chatron-Michaud；Jerome Majcher
    申请人:IFP Energies Nouvelles IFPEN；
    IPC主号:
    专利说明:

    FIELD OF THE INVENTION
    The treatment of certain residues of petroleum refining and distillation units is generally difficult to valorize. Typically the atmospheric residues after distillation under vacuum lead to a vacuum distillate and a vacuum residue. Said distillate is generally catalytically cracked which in turn leads to a residue. A fluidized-bed catalytic cracking unit (FCC) is generally used to convert heavy hydrotreated or non-hydrotreated heavy oil cuts, such as for example a hydrotreated vacuum distillate or a hydrotreated residue, into recoverable petroleum fractions such as propylene gasoline, LPG liquefied petroleum gas or Light Cycle Oil (LCO) which lead to diesel fuel. It remains at the bottom of the catalytic cracking unit a very aromatic residue, this residue has a distillation start point generally around 360 ° C, generally called by the man of trade slurry 360+ cutting. These different residues can be valued in particular as a charge for the production of carbon black.
    Carbon black has applications in various manufacturing processes such as paints, varnishes, lacquers, plastics, fibers, ceramics, enamels, inks of the Indian ink type, as well as certain materials ( rubber for tires in particular). In addition, carbon black has been widely used in the past as carbon paper and black ribbons for typewriters, and now in black electrostatic photocopier powders.
    Carbon black can also be incorporated into some solids to increase their melting point. It is also frequently used as an adsorbent material in purification operations, for example with respect to heavy polyaromatics, or to remove dissolved colored impurities and to fix the suspended material, thus forming impurity aggregates, easy to separate by filtration. Carbon black is also used as a food coloring agent (E152).
    Carbon black is listed in the European Inventory of Commercial Chemical Substances (EINECS) under number 215-609-9. It is classified in several grades according to ASTM D1765.
    PRIOR ART The article "Üpgrade FCC" slurry "oil with chemical settling aids", WF Minyard, World Refining, 01/01/1999, Volume: 9, p 35-38) reports a study on the negative impact of the presence catalyst fines in the residue of a fluidized catalytic cracking unit of a residue (RFCC) during its recovery. A comparison between a cyclone separator and a settling separator with a flocculant chemical is described. This article mentions the interest of having as a charge a very aromatic RFCC residue (obtained by conversion of the very high RFCC) to obtain carbon black oil (CBO), needle cokes ("needle coke"). ), a feedstock for a hydrocracker, or as a component of a commercial heavy fuel oil. Article: "Research progress in purification of FCC" slurry "oil and gas application to Chemical industry" can be translated as "Recent progress in the purification of FCC residues and its applications to the chemical industry" of Bingcheng Cao published in the journal Petrochemical Technology on 01/01/2012 (volume 41, pages 364-369) describes a purification of residues of RFCC to make carbon black oil or coke into needles.The purifications cited are mainly designed to remove catalyst fines: filtration, electrostatic separation, separation by centrifugation, separation by ceramic membrane The valorization of the various residues of the petroleum refining industry is more and more considered, but the valuations described in the art prior art is a simple use as a feedstock for such residues in conversion processes such as RFCC, bubbling bed hydroconversion or by means of a catalyst in suspension, the coking unit or the viscosity reduction unit without an optimization of the quality of the charge that represents said residues is achieved. Therefore the valuation of said residues generally leads to low yields and / or conversions.
    In order to remove impurities from the precursor charge of carbon black to obtain a purer carbon black, thus more recoverable, from a catalytic cracking residue, a hydrotreatment step of said residue is generally carried out but the Output yield of the carbon black unit is modest due to the addition of hydrogen during the hydrotreating step.
    The patent application FR 3,013,717 describes a process for producing carbon black from a "slurry 360+" cut obtained from a fluidized catalytic cracking (FCC) comprising a specific hydrotreatment after the filtration step. of said slurry 360+ cut from an FCC prior to the step of producing carbon black. Said hydrotreatment step makes it possible to increase the yield of the step of producing carbon black and to improve the purity of the carbon black obtained. However, a hydrotreatment is a process operating at high pressure and high temperature requiring the incorporation of hydrogen and which induces a decrease in the quantity of products intended to be the reagents of the carbon black production step.
    Thus, there is a real need for treating residues in order to optimize their use by using them as feedstock in various processes and in particular in processes for the production of carbon black.
    Surprisingly, the Applicant has succeeded in implementing an improved process for producing a composition intended to be used as a filler for a carbon black production step resulting from the combination of at least a part of a residue under vacuum treated specifically in a solvent deasphalting unit and at least one fluidized catalytic cracking residue in a fluidized bed called "360+ slurry" slice, without a hydroprocessing step. More specifically, the Applicant has succeeded in eliminating this hydrotreatment step prior to the carbon black production step by introducing a solvent deasphalting step.
    OBJECT OF THE INVENTION The invention therefore relates to a process for producing a composition for use as a filler for a step of producing carbon black from an atmospheric residue, wherein said atmospheric residue is distilled under vacuum to result in at least one vacuum distillate fraction and at least one vacuum residue fraction, said vacuum distillate fraction being treated according to at least the following two successive steps: • a fluidized catalytic cracking step 1) leading to a residue FCC, a step 2) of filtration of the fine solid particles contained in said FCC residue obtained in step 1) of cracking leading to a filtrate containing less than 300 ppm of particles less than 10 microns, and wherein, said fraction vacuum residue feeds a deasphalting step leading to a deasphalted vacuum residue fraction of which at least a part e mixed with at least a portion of said filtrate obtained in the filtration step 2) to form said composition.
    The composition for use as a filler for a carbon black production step is not hydrotreated.
    An advantage of the present invention is to implement a process operating at moderate pressure and temperature and not requiring the incorporation of hydrogen
    Another advantage of the present invention is the possibility of isolating the most aromatic section of the residue under vacuum by liquid / liquid separation, which does not affect the quantity of products intended to be the reagents of the black production step. of carbon, unlike the hydrotreatment which causes a decrease in the amount of aromatic carbon of the hydrotreated feedstock and thus the amount of carbon black obtained.
    DETAILED DESCRIPTION OF THE INVENTION
    The description of the invention is made with reference to FIG.
    Load
    According to the invention, the feedstock (1) of the process according to the invention is an atmospheric residue of crude oil. The atmospheric residue is obtained following the atmospheric distillation of a crude oil, which can be of very varied origin, and the heaviest part (having a boiling point generally greater than 340 or even 370 ° C.) constitutes the atmospheric residue (1).
    Vacuum distillation
    The feedstock (1) is first introduced into a vacuum distillation column. Two fractions are obtained, a vacuum residue (3) and a vacuum distillate (2). The vacuum distillation according to the invention can be carried out according to all the modes known to those skilled in the art.
    Treatment of vacuum distillate
    In accordance with the invention, the vacuum distillate (2) serves as a feedstock for a fluidized bed catalytic cracking step leading to at least one so-called "360+ slurry" FCC residue (5). The catalytic cracking step can be carried out according to all the modes known to those skilled in the art.
    The vacuum distillate may optionally be sent to a hydrotreatment and / or hydrocracking step prior to the catalytic cracking step. Said hydrotreatment and / or hydrocracking step makes it possible to remove the impurities present in the feed, which makes it possible to obtain cleaner products at the FCC stage outlet.
    Said hydrotreatment and / or hydrocracking step is advantageously carried out according to the techniques well known to those skilled in the art and in the presence of conventional hydrotreating and / or hydrocracking catalysts.
    According to one variant, part of the vacuum residue (3) obtained at the end of the vacuum distillation of the feedstock of the process according to the invention may optionally be added to the vacuum distillate (2) upstream of said step of hydrotreatment and / or hydrocracking.
    According to the invention, said FCC residue (5) obtained at the end of the fluidized-bed catalytic cracking step, called "360+ slurry" slice, is then filtered to yield at least one filtrate (6 ).
    Said filtration step is advantageously carried out according to the techniques well known to those skilled in the art such as the electrostatic filtration technique. The purpose of this filtration is to obtain in the filtrate at a content of less than 300 ppm, and preferably less than 100 ppm in catalyst fines less than 10 microns.
    Treatment of the residue under vacuum
    According to the invention, the vacuum residue (3) resulting from the distillation step of the feedstock of the process according to the invention feeds a deasphalting unit which leads to at least one deasphalted vacuum residue fraction (7).
    Alternatively, residual charges from biomass or coal-based processes (biooils, coal tar) may also be used in admixture with the vacuum residue as co-feed of the deasphalting step.
    The operating conditions of the deasphalting depend on the configuration of the feedstock, the solvents available on the production site as well as the purity and yields expected by the refiner, primarily on the carbon black product. The deasphalting step is carried out by liquid / liquid extraction. The deasphalting step operates at an extraction temperature between 30 ° C and 350 ° C, preferably between 40 ° C and 250 ° C, more preferably between 50 ° C and 200 ° C and the pressure is advantageously ccnprise between 0.1 MPa and 6 MPa.
    The volume ratio of solvent or solvent mixture on the mass of filler is generally between 1/1 and 10/1, preferably between 2/1 to 8/1 expressed in liters per kilogram.
    The deasphalting solvent according to the invention comprises at least one hydrocarbon chosen from saturated hydrocarbons comprising between 2 and 15 carbon atoms and preferably between 2 and 9 carbon atoms, alone or as a mixture. Advantageously, the deasphalting solvent further comprises one or more cycloalkanes, one or more light petroleum fractions of the naphtha type and / or one or more aromatic compounds.
    In the case where the solvent comprises one or more aromatic compounds, said aromatic compound is advantageously chosen from monoaromatic and diaromatic compounds.
    In the case where the aromatic compound is a monoaromatic it is advantageously chosen from benzene, toluene and xylenes alone or as a mixture.
    In one embodiment, the deasphalting is carried out with two solvents and two separate extractors.
    In a second embodiment, the deasphalting is carried out with a double solvent and an adjustment of the ratio between the two extractors.
    In another embodiment, the deasphalting is carried out with a solvent or a constant ratio of two solvents but with a variation of the operating conditions between the two extractors (gradient of T °, pressure, internal extractor, residence time ...). The deasphalting step makes it possible to precisely isolate the most aromatic fraction of the vacuum residue (3) to give a deasphalted vacuum residue (7) which is very concentrated in aromatic carbon, which leads to an increase in the amount of black. carbon that can be produced.
    By aromatic carbon is meant a carbon atom that is part of an aromatic ring.
    Advantageously, a portion of the filtrate (6) obtained at the end of said filtration step may optionally be added to the vacuum residue (3) upstream of said deasphalting step.
    Preparation of the composition for use as a filler for a carbon black production step (8)
    According to the invention, at least a portion of deasphalted vacuum residue (7) is added to at least a portion of said filtrate (6) to yield a composition for use as a filler for a carbon black production step .
    Said composition comprises less than 20% by weight of deasphalted vacuum residue, preferably less than 10% by weight and even more preferably less than 5% by weight.
    According to the invention, the composition does not undergo hydrotreatment before being used as a filler for a carbon black production step.
    DESCRIPTION OF THE FIGURE
    FIG. 1 represents the overall diagram of the method according to the invention. A feedstock (1) is first subjected to vacuum distillation (A), the vacuum residue (3) of which feeds a deasphalting unit (E) to yield a deasphalted vacuum residue fraction (7). The vacuum distillate (2) feeds a fluidized bed catalytic cracking unit (C). The residue of the FCC step (5, "360+ slurry") is filtered (D) then the filtrate (6) and the deasphalted vacuum residue (7) are combined to form the composition (8) according to invention intended to be used as a filler for a carbon black production step not shown in the figure. An optional hydrotreatment step (B) may be performed on the vacuum distillate (2). Part of the vacuum residue (3) can be added to the vacuum distillate (2). Part of the filtrate (6) can be added to the residue under vacuum (3).
    EXAMPLES
    Example 1: Composition comprising a filtered FCC residue and a non-disasylated vacuum residue (non-compliant). Example 1 is non-compliant because the vacuum residue does not undergo deasphalting.
    A middle-type atmospheric residue is distilled under vacuum to give a vacuum distillate and a vacuum residue for separation at 540 ° C.
    The vacuum distillate represents 37% by weight of the atmospheric residue and the residue under vacuum represents 63% by weight of the atmospheric residue.
    The physico-chemical characteristics of the vacuum distillate and the vacuum residue are listed in Table 1 below.
    Table 1
    The BMCI (Bureau of Mines Correlation Index) is defined according to the following formula in which the abbreviation VABP designates the average "volumetric" temperature expressed in rank Rankine and the abbreviation "Sp. Gr" designates the density:
    The vacuum distillate is fed by fluidized bed catalytic cracking (FCC). The operating conditions of the FCC are listed in Table 2, the term C / O corresponds to the ratio of the catalyst flow rate (C) to the feed rate (O), the term ROT corresponds to the exit temperature of the riser and the TRG term is the temperature of the regenerator.
    Table 2
    The yields of the different sections from the FCC, expressed in weight percent, are given in Table 3 below.
    Table 3
    The "360+ slurry" cut is filtered through a passage on an electrostatic filter.
    The physicochemical characteristics of the FCC residue called slurry 360+ after filtration are listed in Table 4 below.
    Table 4
    Filtered "slurry 360+" are mixed with the vacuum residue obtained during the vacuum distillation of the atmospheric residue to form a 97/3 composition by weight, the physicochemical characteristics of which are listed in Table 5 below.
    Table 5
    This composition contains a large amount of sulfur and metals, which would lead to a low quality of carbon black produced.
    Example 2: hydrotreated composition comprising a filtered FCC residue and a non-deasphalted (non-compliant) vacuum residue. Example 2 is non-compliant because the vacuum residue does not undergo deasphalting. In addition, Example 2 is non-compliant because the composition is hydrotreated.
    The composition obtained in Example 1 is treated in a hydrotreatment unit under the operating conditions listed in Table 6 below.
    Table 6
    The physicochemical characteristics of the effluents produced at the outlet of the hydrotreatment unit are shown in Table 7 below.
    Table 7 Hydrotreating greatly reduces the amount of sulfur and moderately the amount of metals. However, the hydrotreatment has the effect of considerably reducing the amount of aromatic carbon, which implies that the amount of carbon black that can be obtained is also considerably reduced.
    Example 3: Composition comprising a filtered FCC residue and a deasphalted vacuum residue (compliant).
    The vacuum residue obtained in Example 1 is sent to a deasphalting unit in two stages.
    The first step is carried out with pentane under a total pressure of 4 MPa, at an average temperature of 170 ° C. and with a volume ratio of solvent to charge mass VSlive / mCharge of 6/1 L-K9'1 ·
    The second stage is carried out with propane under a total pressure of 4 MPa, at an average temperature of 60 ° C. and with a volume ratio of solvent to charge mass VSlive / mCharge of 8/1 L-K9'1 ·
    The physico-chemical characteristics of the deasphalted vacuum residue are listed in Table 8 below.
    Table 8
    The filtered "slurry 360+" obtained in Example 1 and the deasphalted vacuum residue are mixed to form a 97/3 composition by weight, the physicochemical characteristics of which are listed in Table 9 below.
    Table 9
    The proportion of aromatic carbon is greater in the composition obtained in Example 3 according to the invention than in Examples 1 and 2 nonconforming. Thus, the introduction of a deasphalting step makes it possible to increase the proportion of aromatic carbon in the composition intended to be used as a filler for a carbon black production step.
    In addition, although the amount of sulfur is not decreased by deasphalting, the amount of metals is lower in the composition obtained in Example 3 according to the invention. Thus, the carbon black obtained will be cleaner with the use as a filler of the composition obtained in Example 3 than with the use as filler of the composition obtained in Example 1. The deasphalting step makes it possible to to obtain an optimized load for the production of carbon black by avoiding the hydrotreating step and by increasing the amount of aromatic carbon while maintaining a good level of BMCI.
    权利要求:
    Claims (11)
    [1" id="c-fr-0001]
    A process for producing a composition for use as a filler for a step of producing carbon black from an atmospheric residue, wherein said atmospheric residue is distilled under vacuum to yield at least one distillate fraction under vacuum and at least one vacuum residue fraction, said vacuum distillate fraction being treated according to at least the following two successive steps: a fluidized catalytic cracking step 1) leading to an FCC residue, a step 2) of filtering the fine solid particles contained in said FCC residue obtained in step 1) of cracking, resulting in a filtrate containing less than 300 ppm of particles less than 10 microns, and wherein said fraction vacuum residue feeds a step of deasphalting to a deasphalted vacuum residue fraction at least a portion of which is mixed with at least a portion of said filtra obtained in the filtration step 2) to form said composition.
    [2" id="c-fr-0002]
    The production method according to claim 1, wherein said composition comprises less than 20% by weight of deasphalted vacuum residue.
    [3" id="c-fr-0003]
    The production method according to claim 2, wherein said composition comprises less than 10% by weight of deasphalted vacuum residue.
    [4" id="c-fr-0004]
    The production method according to claim 3, wherein said composition comprises less than 5% by weight of deasphalted vacuum residue.
    [5" id="c-fr-0005]
    A production method according to any one of the preceding claims, wherein said deasphalting step operates at an extraction temperature of between 30 ° C and 350 ° C and at a pressure of between 0.1 MPa and 6 MPa.
    [6" id="c-fr-0006]
    6. Production process according to any one of the preceding claims, wherein said deasphalting step operates with a volume ratio of solvent or solvent mixture on the filler mass of between 1/1 and 10/1 expressed in liters. per kilogram.
    [7" id="c-fr-0007]
    7. Production process according to any one of the preceding claims, wherein said deasphalting step operates with a solvent comprising at least one hydrocarbon selected from saturated hydrocarbons comprising between 2 and 15 carbon atoms.
    [8" id="c-fr-0008]
    The production method according to claim 7, wherein said solvent further comprises one or more cycloalkanes, one or more naphtha-type light petroleum fractions and / or one or more aromatic compounds.
    [9" id="c-fr-0009]
    The production method according to claim 8, wherein said aromatic compound is selected from monoaromatic and diaromatic compounds.
    [10" id="c-fr-0010]
    The production method according to claim 9, wherein said monoaromatic compound is selected from benzene, toluene and xylenes alone or in admixture.
    [11" id="c-fr-0011]
    11. Production process according to any one of the preceding claims, wherein said deasphalting step operates with two solvents and two separate extractors.
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    US10336953B2|2019-07-02|
    FR3044319B1|2017-12-22|
    SA116380138B1|2020-12-20|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
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    US20130048537A1|2010-05-07|2013-02-28|Sk Innovation Co., Ltd.|Method of simultaneously manufacturing high quality naphthenic base oil and heavy base oil|
    FR3013716A1|2013-11-27|2015-05-29|IFP Energies Nouvelles|PROCESS FOR PRODUCING CARBON BLACK FROM A MAJOR FCC "SLURRY" CHARGE COMPRISING A SPECIFIC HYDROTREATMENT AND A VACUUM RESIDUE HYDROCONVERSION STEP TO COMPLETE THE "SLURRY" LOAD|
    FR3014897A1|2013-12-17|2015-06-19|IFP Energies Nouvelles|NEW INTEGRATED PROCESS FOR THE TREATMENT OF PETROLEUM LOADS FOR THE PRODUCTION OF LOW SULFUR AND SEDIMENT FIELDS|
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    CA3059217A1|2017-04-07|2018-10-11|Exxonmobil Research And Engineering Company|Resid upgrading with reduced severity fcc processing|
    CN109722299B|2017-10-27|2020-12-04|中国石油化工股份有限公司|Method for producing rubber filling oil from coal tar|
    法律状态:
    2016-11-21| PLFP| Fee payment|Year of fee payment: 2 |
    2017-06-02| PLSC| Publication of the preliminary search report|Effective date: 20170602 |
    2017-11-28| PLFP| Fee payment|Year of fee payment: 3 |
    2019-11-28| PLFP| Fee payment|Year of fee payment: 5 |
    2020-11-26| PLFP| Fee payment|Year of fee payment: 6 |
    2021-11-26| PLFP| Fee payment|Year of fee payment: 7 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1561558A|FR3044319B1|2015-11-30|2015-11-30|OPTIMIZATION OF A DESASPHALTAGE METHOD IN THE OBJECT OF PRODUCING A CHARGE OF CARBON BLACK UNIT|FR1561558A| FR3044319B1|2015-11-30|2015-11-30|OPTIMIZATION OF A DESASPHALTAGE METHOD IN THE OBJECT OF PRODUCING A CHARGE OF CARBON BLACK UNIT|
    CA2950114A| CA2950114A1|2015-11-30|2016-11-25|Optimisation of a deasphalting process with the aim of producing a unit charge of carbon black|
    SA116380138A| SA116380138B1|2015-11-30|2016-11-28|Optimization of a Deasphalting Process with the Aim of Producing a Feed for a Carbon Black Unit|
    US15/363,347| US10336953B2|2015-11-30|2016-11-29|Optimization of a deasphalting process with the aim of producing a feed for a carbon black unit|
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