首页> 外国专利> Zeolith, verfahren zu dessen Herstellung und Verfahren zum Entfernen von Stickoxiden aus Gasen durch selektiven katalytischen Reduktion unter Verwendung des Zeolits

Zeolith, verfahren zu dessen Herstellung und Verfahren zum Entfernen von Stickoxiden aus Gasen durch selektiven katalytischen Reduktion unter Verwendung des Zeolits

机译:沸石,其生产方法和通过使用沸石进行选择性催化还原从气体中除去氮氧化物的方法

摘要

The hydrogen consumption corresponding to the peak of the second wave is equal to a half mole of hydrogen per mole of copper present in the solid. The first wave has two peaks, P1 and P2, resolved by Gaussian deconvolution. The ratio A1/A2 of the zones corresponding to the peaks P1 and P2 respectively are greater than 1.5. Mixed zeolite represented by the formula Cu(x)M'(y)M(z)Z, in which Z represents a zeolitic net with an atomic ratio Si/Al of between 0.9 and 20; M' is lithium and/or a metallic element with a valence of 2, 3 or 4, with an ionic diameter or between 0.12 and 0.30 nm; M is H+, Na+ and/or K+; and x, y, and z are the respective theoretical exchange rates of copper ions and M' and M ions expressed as a percentage of the total exchange capacity of the Faujasite, with the following values: 5=x=60; 20=y=70; z=100-x-y. The zeolite is agglomerated with a link to form grains with a mean size of at least 0.5mm. Z is an X or Y Faujasite. M is a calcium ion, a lanthanide ion or a mixture of lanthanide ions. Process for obtaining such a zeolite, by (a) exchanging some of the exchangeable sites of an M.Z zeolite in powder form with at least a first cation M', (b) agglomeration , (c) exchange of copper for part of the exchangeable cations in the zeolite and (d) heat treatment such as drying and activation. An additional drying and activation stage can be fitted between (b) and (c), or the zeolite can be agglomerated before cation exchange.
机译:对应于第二个波峰的氢消耗量等于固体中存在的每摩尔铜半摩尔的氢。第一波有两个峰,P1和P2,由高斯反卷积分解。分别对应于峰P1和P2的区域的比率A1 / A2大于1.5。由分子式Cu(x)M'(y)M(z)Z表示的混合沸石,其中Z表示Si / Al原子比在0.9和20之间的沸石网; M'是锂和/或化合价为2、3或4的金属元素,离子直径为0.12至0.30 nm; M为H +,Na +和/或K +;和x,y和z分别是铜离子和M'和M离子的理论交换率,表示为八面沸石总交换容量的百分比,其值为:5 = x = 60; 20 = y = 70; z = 100-x-y。所述沸石通过链节聚结以形成平均尺寸至少为0.5mm的晶粒。 Z是X或Y八面沸石。 M是钙离子,镧系离子或镧系离子的混合物。通过(a)用至少一种第一阳离子M'交换粉末形式的MZ沸石的一些可交换位置的方法来获得这种沸石, (d)热处理,例如干燥和活化。可以在(b)和(c)之间安装一个额外的干燥和活化阶段,或者可以在阳离子交换之前将沸石团聚。

著录项

  • 公开/公告号EP1125635A1

    专利类型

  • 公开/公告日2001-08-22

    原文格式PDF

  • 申请/专利权人 CECA S.A.;

    申请/专利号EP20010400283

  • 发明设计人 KIEGER STEPHANE;PLEE DOMINIQUE;

    申请日2001-02-05

  • 分类号B01J29/14;B01J29/06;B01D53/86;B01J29/072;B01D141/00;B01J103/10;B01J103/18;B01J103/26;

  • 国家 EP

  • 入库时间 2022-08-22 01:15:11

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