• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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    • 专利摘要:
    1474728 Recovery of isoprene GOODYEAR TIRE & RUBBER CO 22 Aug 1974 [3 April 1974] 36934/74 Heading C5E Isoprene is recovered, as its azeotrope with n-pentane, from a hydrocarbon stream comprising isoprene, n-pentane and other C 5 hydrocarbons by subjecting the stream to two successive high efficiency distillations, firstly to remove components which are more volatile than the azeotrope as an overhead fraction and secondly to separate the azeotrope as an overhead fraction from a bottom fraction comprising the other hydrocarbons which are less volatile than the isoprene/n-pentane azeotrope. The isoprene-n-pentane mixture can be used to produce cis-1,4-polyisoprene. Acetylenes can be removed from the azeotrope product by hydrogenation or treating with sodium in the presence of an aliphatic alcohol. 1,3-Cyclopentidiene can be removed from the azeotrope product by (a) treating with maleic anhydride and removing the maleic anhydride-1,3-cyclopentadiene adduct by washing with aqueous caustic or flash distillation, or (b) treating with sodium in the presence of an aliphatic alcohol. The hydrocarbon feed can be produced by the steam cracking of naphtha and can be pretreated by being held in a tank under conditions favouring the dimerization of the 1,3-cyclopentadiene so that it is removed more completely during the subsequent distillations.
    公开号:SU740153A3
    申请号:SU742060746
    申请日:1974-09-16
    公开日:1980-06-05
    发明作者:М.Лайбардер Хью
    申请人:Дзе Гуд"Ер Тайр Энд Раббер Компани (Фирма)；
    IPC主号:
    专利说明:

    The present invention relates to a process for the isolation of isoprene from the fraction of petroleum cracking containing pentane. Isoprene is a multi-tonnage monomer for the preparation of polymer products, in particular high molecular weight cis-1, 4-polyisoprene, which is used as a substitute for natural rubber in products such as tires. A known method for the isolation of isoprene from hydrocarbon fractions containing 5 carbon atoms is obtained by rectification of mixtures that contain 72% isoprene and 25% pentane on columns with 30-40 tons. The selected fraction contains 85% isoprene and can be used to obtain high molecular weight polyisoprene 1. However, according to this method, the liquid mixture fractions contain n-pentane in an amount not residual 1 to provide an azeotropic mixture with isoprene, which makes it difficult to release the latter and requires cumbersome expensive equipment. In addition, the application of this method in industry is also limited by the fact that a high reflux ratio is required for the separation of isoprene and other hydrocarbon Cs and therefore a very high steam consumption is required. The proposed method according to the technical essence is the closest method for the separation of isoprene from the fraction Cj of the cracking of petroleum products containing acetylenes and cyclopentadiene by rectification of the mixture. The first extractive distillation removes the main part of cyclopentadiene and acetylene, and then the second hydrocarbon is selectively extracted with a second extractive distillation of the residue from the first distillation. Thereafter, two distillations of the isoprene-enriched stream 2 are produced. The disadvantages of this method are the use of an ECU fraction of hydrocarbons containing isoprene, a large number of operations to remove paraffin and monoolefinic hydrocarbons from isoprene, the duration of the process, the need for additional equipment for regeneration and isoprene, and high equipment investment costs and significant cost of distillation. The aim of the invention is to simplify the technology of the separation process.
    isoprene from the C-Su fraction containing "- Pentane,
     is achieved by the fact that the Cd-Cjj fraction of petroleum products containing R-pentane is subjected to a two-stage rectification with the conclusion of the isoprene-containing fraction as a distillate at the first stage of rectification
    and follow the selection of the azeotropic isoprene-n-peitan mixture containing 25–29% n-pentane in the second stage as a distillate.
     OtIaIchtyoyyggm sign of this
    The method is a simpler technological scheme for the separation of isoprene from the C fraction.
    Conducting a rectification according to this method makes it possible to separate isoprene from various undesirable hydrocarbons, in particular cyclopentadiene and acetylenes. In addition, although various solvents are used in the polymerization of isoprene, but purified n-pentane, which is regenerated with isoprene, is the most convenient solvent.
    Azbtropic admixture contains 73.4% by weight of isoprene and 26.6% by weight of n-pentane. The crude product is isopentane, 1-pentane, 2-methyl-1-butene, isoprene, n-pentane, 2-methyl-2-butene, 1-trans 3-pentadiene, 1-cis-3-G1Tentadiene, cyclopentene, cyclopentane, 2 -methylpentane, 1,4-pentadiene, 1,3-cyclopentadiene, -3-methyl-1-butene, various acetylene compounds in He6bJfbiiioM amount p6dbirguyat
    First Ystytile with the removal of hydrocarbons, more volatile than azeot jupia mixture of isoprene-n-pentane, such as isopentane, 1-pentane, 2-methyl-1-butene, a very small amount of isoprene, H-methyl-1-butene, and 1,4-pentadiene with a small amount of various other saturated and unsaturated C. and C -gluterus, especially acetylenes .. This upper fraction from the first distortion can be selected as gasoline, from which most (if not all) n-pyntana is removed , and thus improve the refined octane. Neither: first fractions from distilled jiliirHH Which contain in base and isoprene, n-pentane, 1,3-pentadiene, cyclopentene, trans-2-pentene, cis-2-pentene, 2-methyl-2-butene, 1,3- cycloenzyme, cyclopenten ,. trans-2-penten, cis-2-pentene, 2-methyl-2-butene, 1,3-cyclrpentadien, cyclopentane, diclo pentadiene, and other hydrocarbons, including other Cg — acetylenes, are then subjected to a second distillation. In the second distillation, the azeotropic mixture of isoprene-n-pentane is taken as the upper fraction, comprising approximately 73% by weight of isoprene and approximately 27% by weight of i-pentane. Sometimes minor amounts may be present in this mixture, usually less than 30 ppm, such as 1,3-cyclopentadiene, isoprin (2J-methyl-1-butene-3-in), 2-butine, 1-penthin and 1-penten-4-in. Due to the nature of the separation (separation of the isoprene-n-pentane aerootropic mixture), the composition of the upper fraction will approach IQ to the composition of the azeotrope enriched in n-pentane. The composition of the top fraction of isoprene-n-pentane can be expressed by a ratio of 65/35 or some other relation compared to the ratio of .. these components in the raw material fed to the second column, as well as to the azeotropic mixture. The highest purity of isoprene for this column, however, is achieved when the composition of the overhead fraction approaches that of composition 0 azeotrope. Lower fractions from the second. distillations containing mainly n-pentane, trans-2-pentene, 2-methyl-2-butene, 2-methylpentene, 1,3-pentadiene and goxane together with small 5 quantities of other Su-hydrocarbons, as well as any dimers 1 , 3-cyclopenyenes, which are less volatile than the azeotropic mixture, can be selected in several ways, Q The bottom fraction from the second distillation can be a hydrocarbon-rubber mixture used in the preparation of other elastomers, hydrogenated and used as an additive to gasoline 5 or as a fuel .
    The proposed method consists in the regeneration of azeotropic mixture of isoprene-n-pentane, as well as other necessary hydrocarbon mixtures.
    Example 1, A mixture of C - Su-coal 0 hydrogens from steam cracking of naphtha is distilled in two stages. At the first stage of distillation, a column with 118 tons is used. Hydrocarbons, more volatile than the azeotropic mixture 5 of isoprene-n-pentane, are removed as an overhead fraction. The lower fractions are subjected to re-distillation on a column with 118 ppm. The azeotropic mixture of isoprene n-pentane is removed as an upper fraction from an excess of n-pentane.
    and other hydrocarbons which are less volatile than the azeotropic mixture and which are removed as lower fractions from the second distillation stage.
    C4-C5-carbohydrate 6p6dy is fed to the column of the first distillation stage at such a rate that the amount of isoprene in the upper fraction is on average 3.2% by weight.
    Composition, weight,%, initial mixture 0. - C, Carboniferous for the first stage of distillation:
    Z-Meail-1-butin0.004
    Isoprin0.07
    2-Butin0.48
    5Z-Methyl-1-butene0.44
    1,4-pentadiene
    Isopentane
    1-penten
    2-Metnl-1-butene
    Izpren
    n-pentane
    trans-2-penten
    cis-2-penten
    2-Methyl-2-butene
    1,3-Cyclopenthalien
    2-Methylpentane
    1-Trans-3-Pentadiene
    3-Methylpentane
    Conditions
    Overhead temperature, С
    Raw and countercurrent temperature
    Temperature at the bottom, С
    Upper pressure, psi
    Average countercurrent ratio
    Composition, wt.%, Upper fraction of the first stage:
    Z-Methyl-1-butin0.01
    Isoprin0.4
    2-Butin2,1.
    Z-Methyl-1-butene2,0
    1,4-Pentadien6,4
    Isopentane52,2
    1-penten 12.6
    2-Methyl-1-butene21,0
    Isoprene3,2 Composition wt.%, (Gizhnaya fraction of the first stage:
    n-Pentane28,6
    2-Methyl-1-butene. :
    Isoprene14,5
    trans-2-penten2,9
    CIS-2-Penten1,4
    2-Methyl-2-butene, 3.7
    1,3-Cyclopentadiene4,7
    2-Methylpentane5,5 3- or 4-Mehil-1-pentene 0.2
    Conditions
    The temperature of the upper fraction, with
    Temperature of raw materials and countercurrent, s
    Bottom temperature, ° С
    Upper pressure, psi
    The average ratio of the flow streams. In the second stage of distillation, an upper fraction is obtained that includes
    No.clopenten
    1-cis-3-pentadiene
    Cyclopentane
    n-hexane
    1,5-Hexalien
    Z-Methyl-trans-2-centen
    Benzene
    T hydrocarbons
    10 Column works for about 16 days at cneAsrrotHHX levels:
    The average
    Measuring range value
    38.1
    37.3
    ; 38.1
    36.1 54.4 55.5
    7.29
    7.35 100/1
    1-trans-3-pentadiene
    5.6
    ,: 3-Methylpentane 1, .9
    0
    Cyclopenten 3.7
    1-cis-3-pentadiene 4.0 2.6
    Cyclopentane
    Hexane 1.8 0.3
    Unknowns
    five
    1,5-Hexadiene 0.4
    2.3 Dimethylbutane 0.2
    2-Methyl-1-pentene
    2-Pentin 0,2
    ЗЧ4етил-Транс-2 -пентен 0,2 1,0
    Benzene
    0
    T yellow (mostly
    18.7
    dicyclopantadiene) nizhni fraction from the first hundred / shchi distillation is then fed to the column of the second stage with such speed,
    5 so that the content of isoprene removed from the bottom should be on average only 1.1%. The column operates for 12 days under the following conditions x1 Range Average measurement value
    43.3
    44.0
    36.2
    38.3 73.0 77.6
    7.41
    7.48 100/1 mainly azeotropic mixture of isoprene 65 -n-pentane. The composition, hours / million, the upper fraction of the second stage: 1-Pentin0,1 Isoprin2.0 2-Butin 2-Methyl-1-butene 0.04 weight Isoprene 74.02 weight n-Pentane 25.91 weight 1, G 1-Pentene-4-i-Cyclopentaleen Composition, wt%, of the lower fractions of the second stage that are to be discarded Isoprene n-Pentane 23,2 trans-2-Pentene 3,4 cis-2-Pentene 1,7 2-Methyl-2- butene 4, 4, 3, 3-Cyclopentene, 2,5 2-Methylpentane6,2 3-or 4-Methyl-1-ne "ten 0.3 1-trans-3-Pentadiene8, 4 3-Methylpentane2.5 Cyclopentene 5,9 1-cis -Z-Pentadiene5,8 Cyclopentan3,4 n-Hexane2,2 2,3-Dimethylbutan0,2 2-Methyl-1-pentene1,0 2-Pentin0,1 Z-Methyl-trans-2-penten0,1 Benzene1.0 T yellow (mostly dicyclopentadiene) 28, 6 Example 2. A mixture of C v sredorodov is distilled in two stages in a distillation unit of example 1. The hydrocarbon mixture, the composition of which is given below, is fed to the first stage distillation with taco. Condition the upper fractions, C Starting material and countercurrent, ° С Lower fractions, с Pressure in the upper column, psig: Average ratio of openings Composition, wt.%, Upper straight unit: Isobutylene0.3 1-Butin 0.3 3-Methyl-1-butin0.02 Isoprin0 , 3 2-Butin1.5 3-Methyl-1-butene5,1 trans-2-Butene0,2 1,4-Pentadibn7,2 cis-2-Butene 0,6 1,3-Butadiene-0.1 Isopentane29.4 1 -Penthene-20.3 ostiness, wh The isoprene light content of light products from the upper peg was an average of 8.7%. The composition, wt.%, Of the starting mixture is Su-carbon 1 species for the first adium: 1-Butene 0.2 G 3-Methyl-1-butine 25 h {mn Isoprin0.1 2-Butine 0.4 Z-Methyl-1-butene 1.5 trans 2-Buten0,1 1,4-Pentadien1,9 cis-2-Buten0,2 1,3-Butadiene; 0,2 Isopentane8,8 1-Penten5,8 2-Methyl-1-butene 6.9 Isoprene 17.5 n -Pentane13.9 trans-2-Penten4,2 cis-2-Penten2,0 2-Methyl-2-butene4,1 1,3-Cyclopentadiene2,4 2-Methylpentane2,1 3- or 4-Methyl-1-penten0, 2 1-trans-2-Pentadien7,3 3-Methylpentane; 0,6 Cyclopentenate; 3,0 1-cis-3-Pentadenene; 4,7 Cyclopentane; 1.3 n-Hexane; 0,7 1,5-Hexadien0,2 2,3-Dimethylbutane; 0,2 2 - Methyl-1-penten0,4 2-Pentin0.05 Benzene .0.4 T jel-e8,9 Column running for 1 4 days of the following conditions: apazon Averages of measurement of 37.6, 6 - 38.7 7.32 04 - 7.43 100/1 1,2-Butadiene 0.7 2-Methyl-1-butene 25.4 Isoprene 8.7 n- PentaneSledy Composition, wt.%, Of the lower fractions of the distillation personalization stage: Isoprene 22.1 n-Penta1n17.0 trans-2-Penten5.8 cis-2-Pentene, s, 4 2-Methyl-2-butene5.3 1,3- Cyclopentadiene1,8 2-Methylpentane, 0 3- or 4-Methyl-1-pentene 6.2
    权利要求:
    Claims (1)
    [1]
    SUMMARY OF THE INVENTION A method for isolating isoprene from a fraction of Cd-C s cracking of petroleum products containing n-pentane using two-stage distillation, with the exception that, in order to simplify the process technology, distillation is carried out with the conclusion at the first stage, as a distillate of a fraction with a boiling point of 3539.С and as a bottoms product of an isoprene-containing fraction, followed by isolation in the second stage of an azeotropic mixture of isoprene-n-pentane containing 25-29% n-pentane as a distillate.
    15.0
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/457,329|US3947506A|1974-04-03|1974-04-03|Recovery of isoprene|
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