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    • 专利摘要:
    1491686 Cyanuric chloride DEUTSCHE GOLD - UND SILBER - SCHEIDEANSTALT 29 Nov 1974 [21 Dec 1973] 51797/74 Heading C2C [Also in Division C1] Cyanuric chloride is made by trimerizing purified cyanogen chloride in the presence of an active carbon catalyst. The cyanogen chloride is purified by passing it over granulated gammaaluminium oxide with an alkali metal or alkaline earth metal content of 0-3% by weight at 20- 100‹ C. (see Division C1). The life of the active carbon catalyst is enhanced by using the purified cyanuric chloride.
    公开号:SU820656A3
    申请号:SU742091498
    申请日:1974-12-20
    公开日:1981-04-07
    发明作者:Гайгер Фридхельм；Хаймбергер Вернер；Шмитт Херманн；Шрайер Герд
    申请人:Дегусса (Фирма)；
    IPC主号:
    专利说明:

    one
    This invention relates to methods for purifying cyanogen and can be used in the preparation of cyanuric chloride by trimerization of cyanogen.
    A known method of purifying cyanogen from water vapor by passing it over a desiccant, in the quality of which a rather aggressive and highly toxic substance is used.
    The closest to the invention to the technical essence and the achieved result is a method for purifying cyanogen in the process of its trimerization on activated carbon by passing cyanogen through a layer of sorbent, which uses calcium sulfate 2.
    The method makes it possible to significantly lower the moisture content of cyan chloride and lengthen the service life of the activated angle.
    However, this method does not allow purification of chlorine cyan from the admixture of aromatic compounds, hydrogen cyanide, the presence of which leads to a reduction in the service life of the activated carbon and the need for its renewal after 6–9 months of operation.
    The aim of the invention is | cleaning of cyan chloride from impurities that poison activated carbon, as well as an increase in the service life of the latter.
    The goal is achieved by the proposed method of purifying chlorocyan while the latter is trimerized on activated carbon by passing chlorocyan through a layer of sorbent, which uses granulated α-alumina containing 0.01–3.0% of alkali and alkaline earth hydroxides, and 20-100 C. At the same time, y-alumina is regenerated by passing air at 200-600 ° C and returns to the process;
    The hallmark of the method
    0 is the use as a sorbent of γ-alumina with a certain content of hydroxides of alkali and alkaline earth metals, the conditions of the process,
    5 and the conditions for regeneration of | f-alumina.
    . The technology of the method is as follows.
    权利要求:
    Claims (2)
    [1]
    Technical chlorine cyanide, containing up to 0.7 wt.% Water, hydrogen cyanide, chlorine and chlorine derivatives of benzene, is passed at 20-100 ° C, preferably but at 30-60 ° С, through - alumina, holding 0.01-3 , 0 wt.% Hydroxides of alkali or alkaline earth metals. The size of the grains) j is chosen in such a way that an economically unprofitable velocity head does not arise. The treatment time is 1-600 s, preferably 1-60 s. Chlorine cyanide after this treatment contains 0.02 wt% water and, according to gas chromatography, does not contain any impurities of benzene and its derivatives, as well as hydrogen cyanide, as a result of which subsequent trimerization of the resulting cyanogen on activated carbon does not reduce the activity of the latter during 12 I The alumina is regenerated by heating to 200-600 ° C, preferably 350-400 while passing air, and is returned to the process again. After 17 cycles of operation, y-oxide still retains sorption activity. Example. A glass tube with a diameter of 9 mm and a length of 250 mm FILLING 15T 12g y - Ap2-z {density 250 m / g, pore size 90 A °, alkali content 0.05 wt.%, Grain size 2-3 mm), is heated to 60 18 g of a gaseous chloro cyan containing, in wt.% T, 0.7 water, 0.08 hydrogen cyanide, are passed through C for 1 hour; 0.1 benzene and 5.0 chlorine. The water content after purification is less than 0.02%, and no impurities of the remaining components are detected. After cleaning, 350 g of cyanogen chloride-alumina are regenerated in air flow at 500 ° C. EXAMPLE 2. Two parallel-connected nickel tubes with a diameter of 50 mm and a length of 2000 mm fill 2.8 kg (density 360, alkali content 0.6 weight, grain size 5-7 mm), heat one of the tubes to 35 ° C and miss 2.6 kg of chlorian cyan containing, weight. 0.2-0.3 water 0.05-0.06 benzene and 3 3.5 chlorine. After 72 h, the cleaning process is switched to the second tube, and the first tube is switched to regeneration at 350–400 ° C for 2 h by passing air. The resulting cyanogen is sent for trimerization at З50s on activated carbon. The use of the invention allows to increase the service life of coal to more than 12 months. Example 3. The method is carried out by analogy with that described in Example 1, but chlorocyan gas is used, which instead of benzene contains 0.1% by weight of a mixture consisting of benzene, chlorobenzene, 1,2 - dichlorobenzene and 1,2, 4 - trichlorobenzene. The analysis showed that chlorocyan treated with U-alumina contains less than 0.02 wt.% Of water and does not contain (in detectable amounts) neither hydrogen cyanide nor the initially aromatic compounds present. Even the 17-time regeneration and subsequent use in each case of α-alumina showed no loss of activity. Claim 1. Method of purifying chlorocyan in the process of its trimerization on activated carbon by passing through a layer of sorbent, characterized in that, in order to purify chlorocyan from impurities, poisoned kmtsi activated carbon, and increase the service life of the latter, as a sorbent, granulated y - alumina containing up to 0.01-3.0 wt.% hydroxides of alkali and alkaline earth metals, and cleaning is carried out at 2 ~ 10 ° C, followed by regeneration of the sorbent. 2. A method according to claim 1, characterized in that y-alumina is regenerated by passing air at 200-600 s and returned to the process. Sources of information taken into account in the examination 1. For the Germany of Germany 204786, cl. 12p 10/05, 1973.
    [2]
    2. For the Germany FRG 2045823, cl. 12p 10/05, 1973.
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    同族专利:
    公开号 | 公开日
    IL46204A|1977-07-31|
    DK143266B|1981-08-03|
    NL7414996A|1975-06-24|
    DD115641A5|1975-10-12|
    DK660974A|1975-09-01|
    HU170259B|1977-05-28|
    CA1034056A|1978-07-04|
    FR2255260A1|1975-07-18|
    DK143266C|1981-12-21|
    CH607984A5|1978-12-15|
    SE398340B|1977-12-19|
    JPS5096495A|1975-07-31|
    FR2255260B1|1977-05-20|
    US3949060A|1976-04-06|
    JPS5813493B2|1983-03-14|
    IL46204D0|1975-03-13|
    ATA1020774A|1976-04-15|
    DE2363867A1|1975-09-04|
    BE823608A|1975-06-19|
    DE2363867B2|1977-03-17|
    SE7414627L|1975-06-23|
    IT1024767B|1978-07-20|
    RO66454A|1979-01-15|
    AT333786B|1976-12-10|
    GB1491686A|1977-11-09|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    GB674813A|1949-12-12|1952-07-02|Degussa|Process for the production of cyanogen chloride|
    US2774744A|1950-11-06|1956-12-18|Grace W R & Co|Method of preparing low soda-content alumina catalyst|DE2931353C2|1979-08-02|1982-06-09|Degussa Ag, 6000 Frankfurt|Process for the purification of raw, hydrous cyanogen chloride|
    DE3103963A1|1981-02-05|1982-08-19|Skw Trostberg Ag, 8223 Trostberg|Process for preparing cyanogen chloride|
    CA1208141A|1982-12-20|1986-07-22|Charles R. Nease|Removal of carbon dioxide from olefin containingstreams|
    CN109289820B|2018-10-30|2021-03-19|山西新华防化装备研究院有限公司|Method for treating activated carbon after adsorbing cyanide|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE19732363867|DE2363867C3|1973-12-21|Process for purifying cyanogen chloride|
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