• 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:
    A process for the separation of carbon black nanoparticles from a polyolefin resin. The present invention relates to a process for the separation of carbon black nanoparticles from a polyolefin resin. Said process is characterized in that it comprises the step of packaging diatomite with a particle size between 5 and 100 μm in a chromatographic column to obtain a density of 0.1 to 1.0 g/cm3 The chromatographic column is then heated to a temperature of at least 120ºC. After that, 0.01 to 0.30% w/v hot polyolefin solution is added to the column. Next, the organic solvent is added to the column and the leaving polyolefin solution is collected. (Machine-translation by Google Translate, not legally binding)
    公开号:ES2602252A1
    申请号:ES201630450
    申请日:2016-04-11
    公开日:2017-02-20
    发明作者:Worawat Chuencheep；Piyada LERDPRAPAPONG；Kataguna KANOKNUKULCHAI
    申请人:PTT Global Chemical PCL；
    IPC主号:
    专利说明:

    The present invention discloses a process for the separation of carbon black nanoparticles from a polyolefin resin, characterized in that said process comprises the following steps:
    (a) pack diatomite with a particle size between 5 and 100 µm in a column
    chromatographic until a density of 0.1 to 1.0 g / cm3 is obtained; 10 (b) heat the column to a temperature of at least 120 ° C;
    (C) add 0.01 to 0.30% w / v of the hot polyolefin solution to the column;
    (d) add organic solvent to the column, and collect the polyolefin solution that comes out. Field of the Invention
    The present invention relates to a chemical process, especially to the part of the process for the separation of carbon black nanoparticles from a polyolefin resin. Background of the Invention Carbon black is an important additive for polyolefin resins in the
    20 production of high pressure water pipes. Carbon black can be used as a lightweight polyethylene stabilizer. On the other hand, it can also be used as a colorant and conductive additive for polyolefin.
    For research and development of polyolefins that have good properties, gel permeation chromatography (GPC) is an important technique for the analysis of molecular weight and microstructure of the polymer, resulting in a polymer synthesis
    with a desired weight or molecular microstructure.
    However, the analysis of the polyolefin resin comprising carbon black by GPC cannot be performed directly because the carbon black has a size of nanoparticles that can become clogged and cause damage to the GPC column. Further,
    30 carbon black causes interference with the analysis, causing errors in the result obtained. For these reasons, separation of carbon black from the polymer before analysis is extremely important. Direct filtration of the mixture of carbon black and hot polyolefin using filtration equipment was disclosed in U.S. Patent Nos. 3,232,891, 4,123,235 and
    35 4,295,867. Said separation process has the disadvantage that the black size of
    Carbon that has nanoparticles gets through the filter paper. Moreover, be 2


    He checked that part of the polyethylene can be removed by filtration with carbon black. This causes crucial errors in the analysis of the molecular weight of the polyolefin from the separation.
    Centrifugation to separate carbon black from a resin of
    5 polyolefin while hot cannot provide good efficiency, because part of the carbon black with a nanoparticle size cannot sediment and is separated from the polyolefin solution.
    For these reasons, this invention aims to separate carbon black nanoparticles from a polyolefin resin for the analysis of the molecular weight and microstructure of the polyolefin by the GPC technique.
    Detailed description of the invention
    This invention describes a process for the separation of carbon black nanoparticles from a polyolefin resin for polyolefin analysis by the GPC technique, which can be described according to the following embodiments.
    Any aspect shown in this document is intended to include other aspects of this invention, unless otherwise indicated. All technical and scientific terms used in this document have the meaning understood by those skilled in the art, unless otherwise defined.
    20 Any instrument, device, method or chemical mentioned in this document, unless otherwise indicated, means any instrument, device, method or chemical that the person skilled in the art in this field uses or generally implements , unless it is indicated that they are specific tools, devices, methods or specific chemicals exclusive to this invention.
    The use of singular names or pronouns when used with "comprising" in the claims and / or in the specification, means "one" and will also include "one
    or more "," at least one ", and" one or more than one. "All the compositions and / or methods described and claimed in this application are intended to cover aspects of the invention obtained from the embodiment,
    Operation, modification, or variation of any factor without experimentations that are significantly different from this invention, and the same are obtained that have properties, utilities, advantages and results similar to aspects of the present invention according to those skilled in the art even without which is specifically indicated in the claims. Therefore, substitution or similarity with aspects of this
    The invention, including any modification or minor change that may be evident to the person skilled in the art in this field will be considered under the intention, concept and scope 3


    of this invention, as it appears in the appended claims.
    Throughout this application, the term "approximately" used to indicate any value that appears or is expressed in this document may be varied or modified, variation or modification that may be the result of the error of the instruments and
    5 methods used to determine various values. Embodiments of the invention are shown below with no intention of limiting any scope of the invention. This invention relates to the process for the separation of carbon black nanoparticles from a polyolefin resin, characterized in that said process 10 comprises the following steps:
    (to) pack diatomite with a particle size between 5 and 100 µm in a chromatographic column until a density of 0.1 to 1.0 g / cm 3 is obtained;
    (b) heat the column at a temperature of at least 120 ° C;
    (c) adding 0.01 to 0.30% w / v of the hot polyolefin solution to the column; 15 (d) add organic solvent to the column, and collect the polyolefin solution that comes out. In one embodiment, the preferred diatomite has a particle size between 30 and 50 µm. In one embodiment, the density of the diatomite packed in the column is between 0.1 and 1.0 g / cm 3 and preferably is between 0.3 and 0.5 g / cm 3.
    In one embodiment, the diatomite packaging step in the chromatographic column may be selected from, but not limited to dry or suspended packaging, or it may be packaged with a combination of dry and suspended packaging.
    In step (a) of diatomite packaging, you can also comprise washing diatomite by letting the organic solvent pass through the column.
    In one embodiment, in step (b), the column is heated to a temperature of at least 120 ° C. Preferably, the temperature of the column in step (b) is between 130 and 150 ° C.
    In one embodiment, the concentration of the hot polyolefin solution in the step
    (c) is between 0.01 and 0.30% in w / v, preferably it is between 0.05 and 0.15% in w / v. Preferably, the temperature of the hot polyolefin solution in step (c) is in a range not less than or not greater than 10 ° C of the temperature of the column in step (b).
    In one embodiment, the volume of the organic solvent added in step (d) is 4


    1 to 3 times the volume of the hot polyolefin solution in step (c).
    At each stage of the process for the separation of carbon black nanoparticles from a polyolefin resin according to this invention, unless specified, the organic solvent in any of each of the stages can be
    5 select from haloaromatic hydrocarbons or a mixture of said organic solvents. Preferably, the organic solvent may be selected from 1,2,4-trichlorobenzene (TCB), orthodichlorobenzene (oDCB), or a mixture of said organic solvents.
    In one embodiment, the polyolefin resin can be selected from, but is not
    10 limited to, polyethylene, polypropylene, polyethylene copolymer and an α-olefin having from C3 to C20, polypropylene copolymer and an α-olefin having from C4 to C20, or a mixture of said polyolefin resins.
    The following examples are only intended to explain the present invention, and not be a limitation of this invention in any way. 15 Carbon black separation from a polyolefin resin through a comparison process
    The separation of carbon black from a polyolefin resin by a comparison process was initiated by dissolving the polyethylene resin in 1,2,4-trichlorobenzene solvent (TCB) at a temperature of 130 150 ° C until a concentration of
    20 polyethylene of 0.1% w / v approximately. The filtration is then carried out by pumping the solution prepared to pass through the 1 µm filter equipped with Agilent PLSP 260VS at a temperature of 140 150 ° C and collect the filtrate and analyze the amount of carbon in the filtrate using thermogravimetric analysis (TGA) . Carbon black separation from a polyolefin resin using the process of
    25 This invention The separation of carbon black from a polyolefin resin using the process of this invention can be done by packing glass wool and diatomite (Celite® 545) on a chromatographic column having a diameter of 1 cm. The density of the diatomite in the column was between 0.350.5 g / cm3. That column was heated to 130
    30 150 ° C and the diatomite was washed with 20 ml of 1,2,4-trichlorobenzene (TCB) at the same temperature. Then, 0.050.15% w / v of the polyethylene / butane copolymer sample composed of carbon black in a solution of 1,2,4-trichlorobenzene was added to the column at the same temperature, rinsed with organic solvent , and the solution passing through the column was collected and analyzed for the amount of carbon using
    35 thermogravimetric analysis (TGA). Quantitative analysis of carbon black in the polymer using TGA 5


    The amount of carbon black can be analyzed using the NETZSCH TG 209 F1 Libra® Thermogravimetric Analyzer under the following conditions.
    Table 1 shows the conditions of quantitative carbon black analysis using thermogravimetric analysis (TGA).
    Experimental conditions
    Temperature range (ºC) Thermal gradient (ºC / min)Gas (Feed Rate)
    one 25550twentyN2 (20 ml / min)
    2 550900twentyO2 (20 ml / min)
    5Analysis of the molecular weight of polyolefin by GPC
    The molecular weight of the polyolefin was determined by Polymer Char gel permeation chromatography (GPC) using the IR detector and column 3 PLgel 10 µm MIXEDB. The analysis was performed at 140 ° C using 1,2,4-trichlorobenzene as the solvent
    10 rinse and using the test method of ASTM D6474. Effect of carbon black filtration and result of molecular weight analysis Table 2 shows the amount of carbon black in a polyethylene solution before and after filtration.
    Polymer example Amount of carbon black in the polymer solution (% by weight)
    Polyethylene resin 0.0
    Polyethylene resin composed of carbon black 2.2
    Filtered through Celite® 545 0.0
    Filtered through 1 µm filter (1 time) 1.6
    Filtered through 1 µm filter (2 times) 1.2
    15 Table 2 and Figures 15 show the results of the quantitative analysis of carbon black in the polyethylene resin using TGA. From the analysis, it was found that the carbon black separation process from a polyolefin resin according to the invention that must be filtered through Celite® 545 can eliminate all the
    20 carbon black in the polyethylene sample. Notwithstanding the separation of carbon black


    According to the comparative experiment that is filtered through a 1 µm filter, you cannot remove all carbon black from the polyethylene, despite filtering twice. Results of the molecular weight analysis of the polyolefin solution after
    5 carbon black separation
    Table 3 and Figure 6 show the result of the analysis of the molecular weight of the polyethylene resin which is not composed of carbon black and polyethylene resin composed of carbon black after filtering with Celite® 545 using GPC. It was found that the polyethylene from which carbon black had been removed using Celite®
    10 545 and polyethylene with the same quality that had not been composed with carbon black showed no significant difference in the characteristics of molecular weight and molecular weight distribution. Therefore, it can be summarized that the separation of carbon black from a polyethylene resin using the process according to the present invention can separate the carbon black from the polymer without causing errors in the analysis
    15 molecular weight of the polymer after separation. Table 3 shows polyethylene resin that has not been composed with carbon black and polyethylene resin composed of carbon black after filtration with Celite® 545.
    Mn P.mMzMWD
    Carbon black polyethylene resin 9713236,9081,280,34424
    Composite polyethylene with carbon black filtered through Celite® 545 10376234,1611,165,1722. 3
    20 Brief description of the drawings Figure 1 shows the% by weight of carbon black in the polyethylene resin using the TGA technique. Figure 2 shows the wt% carbon black in the carbon black composite polyethylene resin using the TGA technique.
    Figure 3 shows the weight% of carbon black in the carbon black composite polyethylene resin after filtration with Celite® 545, using the TGA technique.
    Figure 4 shows the% by weight of carbon black in the carbon black composite polyethylene resin after filtration with a 1 µm filter, using TGA technique 30.


    Figure 5 shows the weight% of carbon black in the carbon black composite polyethylene resin after filtering with a 1 µm filter for the second time, using the TGA technique.
    Figure 6 shows the molecular weight of carbon black free polyethylene resin 5 and carbon black composite polyethylene resin after filtration with Celite®
    545
    Best mode of the invention
    The best mode or preferred embodiment of the invention is as indicated in the description of the invention. 10

    权利要求:
    Claims (9)
    [1]
    1. A process for the separation of carbon black nanoparticles from a polyolefin resin, characterized in that said process comprises the following steps:
    5 (a) pack diatomite with a particle size between 5 and 100 μm in achromatographic column until a density of 0.1 to 1.0 g / cm3 is obtained;
    (b) heat the column at a temperature of at least 120 ° C;
    (C) add 0.01 to 0.30% w / v of the hot polyolefin solution to the column;
    (d) add organic solvent to the column, and collect the polyolefin solution that comes out.
    [2]
    2. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the diatomite has a particle size between 30 and 50 µm.
    [3]
    3. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the density of the diatomite in the column in step (a) is between 0.3 and 0.5 g / cm3.
    The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the temperature of the column in step (b) is between 130 and 150 ° C.
    [5]
    5. The process for the separation of carbon black nanoparticles from a
    The polyolefin resin according to claim 1, wherein the concentration of the hot polyolefin solution in step (c) is between 0.05 and 0.15% w / v.
    [6]
    6. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the temperature of the
    The hot polyolefin solution in step (c) is in a range not less than or greater than 10 ° C of the column temperature in step (b).
    [7]
    7. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the volume of the organic solvent added in step (d) is 1 to 3 times the volume of polyolefin solution
    hot on stage (c).9

    [8]
    8. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the organic solvent in any of each of the stages is selected from haloaromatic hydrocarbons or
    5 a mixture of said organic solvents.
    [9]
    9. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 8, wherein the organic solvent is selected from 1,2,4-trichlorobenzene (TCB), orthodichlorobenzene (oDCB), or a mixture of
    10 said organic solvents.
    [10]
    10. The process for the separation of carbon black nanoparticles from a polyolefin resin according to claim 1, wherein the polyolefin resin is selected from polyethylene, polypropylene, polyethylene copolymer and an αolefin having
    15 from C3 to C20, polypropylene copolymer and an alpha olefin having from C4 to C20, or a mixture of said polyolefin resins.


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    同族专利:
    公开号 | 公开日
    ES2602252B2|2017-07-20|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3276995A|1963-05-29|1966-10-04|Du Pont|Process for the removal of dispersed carbon particles from an aqueous media|
    US4191542A|1975-03-31|1980-03-04|Phillips Petroleum Company|Filtering process for a carbon black-containing gas|
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