• 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 preparing 1,1,1-trifluoro-2,2-dichloroethane by hydrofluorination, in the gas phase, of perchloroethylene in the presence of a catalyst comprising chromium oxides supported on AlF3 in the gamma and/or beta form.
    公开号:SU1706385A3
    申请号:SU884355357
    申请日:1988-03-09
    公开日:1992-01-15
    发明作者:Кармелло Диего；Гульельмо Джорджио
    申请人:Аусимонт С.П.А. (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to a method for producing a 1,1,1 -m reef torus-2, 7. -dichloroethane, which is used as a liquid for aerosols, as a propellant of organic synthesis.
    The purpose of the invention is to increase the yield of the target product.
    The number of moles pdlu chenndgd p (edduct
    Mole number of converted raw material
    For a better understanding, the output is 1,1,1-trifluoro-2 output intermediate and duct. According to the invention, the stroke means expressed
    and the net yield of by-products is very low (about 10%).
    Example 1A. g of aluminum trifluoride consisting of delta-AlFj, 60% gamma-A1P3 and $ 10 from beta-A1G5 and alpha-A1P3, is impregnated with a solution prepared by dissolving 52.3 g of CgSC bK20 in 58 ml of distilled water. Trifto For a better understanding, consider the yield of 1,1,1-trifluoro-2, 2-dichloroethane, the yield of intermediate and side products. According to the invention, the term output means the expression
    )
    about
    ABOUT)
    with
    CS SL
    The aluminum reed is composed of particles with a diameter of 20–7.00 µm, an average diameter of 8 µm. Aluminum tri-oxide is impregnated, Cr 2 C 1 3 H O with stirring; then the catalyst is partially dewatered in an oven at 110 ° C for 1.5 hours, after which it is placed in a tubular inconel reactor with an inner diameter of 5 cm, you are CM
    i
    . I NO SI and nmgori (.n; i H, (-the chains of porous membranes -, about log; - foam from the mix 1 to evenly distribute gases coming from the bottom and to support the inactive catalyst layer. Thermocouples for temperature measurements are placed in oboloyku measured in the middle suit of the reactor.
    The catalyst, placed in the described reactor, is heated to 20 ° C in a stream of nitrogen of 100 l / h; the nitrogen flow is stopped and 100 l / h of air and 80 l / h of HF are sent to the reactor after they are respectively mixed in a heat exchanger located upstream of the reactor. Heating is resumed in air flow and HF until it reaches 40 ° -9 °. This temperature is subdued under At. H, after which the catalyst is cooled in a stream of nitrogen.
    PRI me R 1B. The catalyst thus obtained is used and the same apparatus, 0.855 mol / h and 3 mol / h HF, are sent to the reactor. The reaction temperature is ZbP ° C and the pressure is slightly above atmospheric. The contact time is 5 s, which is calculated as the ratio between the non-fluidized volume of the catalyst and the volumetric flow of the reactants supplied at the reaction temperature and pressure. The gases leaving the reactor are removed for 1 hour. After absorption of HCl and HF in water and after washing the reaction product with an aqueous solution of NaOH, g of product is obtained, the molar composition of which is as follows,%:
    CFjCHCIF1,2 CF -CHCli 5.1 CC1 CC1F + CC1F2-CHC12 5.0 CgCl4 88.0
    The conversion is 2%, while the yield of CP3-CHC1t. 2.9% and yield
    BY-PRODUCTS 10%.
    Example 1B (comparative tests). Aluminum trifluoride used to prepare the catalyst in Example 1 is introduced into the apparatus of Example 1. At a reaction temperature of 3 0 ° C and a pressure slightly above atmospheric, 0.886 mol / h of C2C14 and H, mol / h of HF are fed. After pro0
    0
    L-,
    ,
    s 5
    0
    J
    uecca, an analogue of the process described in Example B, gives g of a reaction product having the following molar composition,%:
    ClFj - C1 C12Foots
    .F + Cf; lI-2 (; nci21.1
    SgS1498,5
    Therefore, aluminum trifluoride as such is not suitable for producing CF3-CHC12.
    Example 2A. g of aluminum trifluoride, consisting of gamma-AlFj and having a surface of 28 m / g, is impregnated with a solution obtained by dissolving 52.3 g of CrCl j in 58 ml of distilled water. Impregnation and dewatering are similar to Example 1. The dehydrated catalyst was introduced into the reactor of Example 1 and heated to 5 ° C with air at a flow rate of tCD l / h. It is maintained at this temperature until only traces of chloride ions are detected in the washing solution of the air leaving the reactor. Then the catalyst is cooled with nitrogen. The number hrsma related to the catalyst, 3 wt.3.
    Example 2b The catalyst of the winner / A (g) is introduced into the apparatus of example 1. At a reaction temperature of Zb1) ° C and a pressure slightly above atmospheric, 0.925 mol / h of CzCl is fed. and 3, / 55 mol / h HF. After 1 h, g of reaction product is obtained, the molar composition of which is as follows,%:
    CFyCHCIF9
    CF3-CHCl2.15,9
    CC1 CC1F + CC1F2CHC125, 7
    45
    Jq
    C, C1
    64.0
    The transformation. 3 &%, yield CF3CHC1Z M $, yield of by-products 25%.
    Example Using the catalyst of example 2, the apparatus of example 1, the reaction temperature of ZCHO ° C and the pressure slightly above atmospheric, 0, mol / h C2C14 and 9.725 mol / h HF are fed. The process is carried out for 1 hour; 153 g of a reaction product is obtained having the following molar composition,%:
    CF3 - CHC1F ..4,8
    CFs-CHCli14,8
    CCL2 CC1F + CC1F2СНС1г 7,4
    C2C1471.0
    ronr
    29 ,, h move
    With L h j LiiCl 5 1 Ј AND OUTPUT SIDE BY. Ob
    duc tov 1 k i ,.
    Example A. g of trifluoride alochl, containing 80% gamma-AN, having a surface area of 18 mg / g, was soaked for the first time with a solution obtained by dissolving 5-, 3 g of CrCl x 6H20 in 58 ml of distilled water. The impregnation and dewatering process is the same as in Example 1. After dewatering, the catalyst was then popitalized a second time with the same amount of chromium solution having the same concentration until a chromium content of 6% by weight was obtained.
    The catalyst is dried again, introduced into the reactor of Example 1 and treated with a stream of nitrogen (100 m / h) saturated with steam at 0/500 ° C. The treatment was carried out at ZbO ° C until only traces of chloride ions remained in the solution for washing the nitrogen leaving the solution. Then dehydrated with dry nitrogen.
    Example B. The catalyst of example A (g) is placed in the apparatus of example 1. At a reaction temperature of 30) C and a pressure of atm above atmospheric, it is fed - 0.801 mol / h and, G / 1 mol / h HF. After 1 hour of treatment, 130 g of the product of the reaction of the molar composition D is obtained:
    CF3 - CHC1F2,2
    CF3 - CHC1211, 2
    CC12 CC1F +
    + CC1F2-CHC128,1
    SgS14
    76.7
    The C2C14 conversion is 23.3%, the yield of CFjCHCl .; 8.1% and the output of by-products e, l%.
    EXAMPLE 5A (comparative tests). A solution of 10 kg of dodecahydate chromium-alum alum (KCr (SO.) 2. 12H20) in 71.5 liters of water is added at room temperature and stirred with an aqueous solution of ammonium hydroxide, containing about 10 wt.% KNz until the pH reaches 8, eight. The suspension of chromium hydroxide is then stirred for 30 minutes at room temperature, taking into account that the pH remains between 8.8 and 9.0 added, if necessary, additional amounts. The suspension is then diluted with deionized water to a volume of 1B, then decanted for 2 hours, optionally
    five
    0
     ABOUT USE OF G / T. LN. P and T -.Ch.1.
    flocculating,) gontl (.-er, can be used 1 (: with SOP. AN).
    The greatest. the colic :: your aqueous phase is copied and the operation is repeated (dilution with
     washing) three more times. After filtration, the filter cake cake of chromium hydroxide is suspended in deionized hot water (85-9 ° C); 1750 g of product containing 15Ј of solid product suspended in 3 ml of water. The hot rinsing is repeated several times until the concentration of sulfate ions (S04) is lower than 0 wt.% With respect to the calcined dry product. Finally, the press-cake cake of chrome hydroxide is suspended again in 3 liters of acetone at room temperature, thereby obtaining filtration of chromium hydroxide, which is activated in a muffle furnace in accordance with the following 5 schedule: 5 hours at 100 ° C; 2 hours at 00 ° C, L-5 hours at 500-550 ° C.
    Received dark green granules having an ion content of 50 below 0, wt. C and specific surface area RB m2 / g.
    Example 5B. The apparatus of example 1 is injected (60 g of a catalyst based on chromium oxide according to example 5A in granules at a reaction temperature of 320 ° C and a pressure slightly above atmospheric, 1.163 mol / h of C2TC and 3 mol / h of HF are fed. After 1 h of treatment, g of the reaction product of the following molar composition,%:
    CF3CHF2Y
    CFjCHCIF6,1
    CF3CCl2.F4,6
    CF3CH2C111.2. CF3CC1ZH 19.9
    CC12 CC1P +
    + CC1P2-CHC1g2
    C2Cl4.32,1
    The transformation. 66.9%, CF yield, -CHC12 29.7% and non-recyclable by-products 67%.
    Example 6. Following the procedure described in example 1, a catalyst was prepared consisting of A1F (30% delta-A1P3, 60% gamma-AlFj and 10% beta-AlFj) and including Cr20} in an amount corresponding to 8 mol% based on AlF and was used in the form of a bed in a reactor, similar to the reactor used in Example 1
    0
    five
    0
    five
    0
    five
    for the reaction of a mixture of Cj - i-Wr, in uyol oiih:
    Temperature
    reaction, Contact time, s 1.98 Feed rate miol / h 12 Feed rate of HF, mmol / h 63 Reaction time, h 6 Reaction products are extracted, as in Example 1. The composition of products is as follows:
    CF3CHC1F14, A CP CHC1g 25.5 3.5 CF2C1-СНС12 0.3 Light products 25.2 Unreacted 27.4 Conversion C2C14 72.6, output CF CHClfc
    The invention allows to significantly increase the yield of the target product to 3.6 - 51%, against 2Q% in the prototype, and to reduce the formation of by-products to $ 25, against -0-703; respectively in the prototype.
    0
    five
    F o r c u l a geni
    The method of obtaining 1,1, 1-trifluoro-2, .- dichloroethane by reacting tetrachlorethylene with hydrogen fluoride in the gas phase at COO-ZBS C in the presence of a chromium oxide-based catalyst. In order to increase the yield of the target product, as a catalyst, a catalyst is used, which is chromium oxide, deposited in the amount of masts based on chromium on aluminum fluoride in a gamma form or in a mixture of gamma and beta forms with the possible presence of no more than jd% delta form with an area aluminum fluoride surfaces 1.8 - 28 M2 / g obtained by impregnating aluminum fluoride with a solution of chromium salt, followed by drying the catalyst and activating it with air or nitrogen saturated with steam, at 200- 500 ° C, and the process is carried out at a molar ratio of hydrogen fluoride and tetrachlorethylene equal to (3- U): 1.
    权利要求:
    Claims (2)
    [1]
    The method of obtaining 1,1,1-trifluoro-
    [2]
    2, .- of dichloroethane by the interaction of tetrachlorethylene with hydrogen fluoride in the gas phase at COO-CBS C in the presence of a catalyst based on chromium oxide, which differs ) 0 C in that, in order to increase the yield of the target product, use as a catalyst the catalyst is chromium oxide deposited in an amount of 3 _ 8 wt.% based on chromium on aluminum fluoride in gamma form or in a mixture of gamma and beta forms with the possible presence of not more than 30% delta form with a fluoride surface area aluminum 1.8 - 20 28 m 2 / g obtained by feeding aluminum fluoride ^ with a solution of the chromium salt, followed by drying the catalysis and activating it with air or nitrogen saturated with water vapor,
    25 at 200-450 ° C, and the process is carried out at a molar ratio of hydrogen fluoride and tetrachlorethylene equal to (3-10): 1.
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    引用文献:
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    IT19622/87A|IT1202652B|1987-03-09|1987-03-09|PROCESS FOR THE PREPARATION OF 1,1,1-TRIFLUORO-2,2-DICHLOROETHANE BY HYDROFLUORATION IN THE PRESENCE OF CATALYSTS|
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