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    • 1. 发明授权
    • Method for purification of phenol
    • 苯酚纯化方法
    • US5502259A
    • 1996-03-26
    • US290258
    • 1994-08-15
    • Vladimir M. ZakoshanskyIrina I. VasilievaAndrei K. Griaznov
    • Vladimir M. ZakoshanskyIrina I. VasilievaAndrei K. Griaznov
    • B01J29/06B01J29/08B01J29/18B01J29/20B01J29/65B01J35/10C07B61/00C07C37/08C07C37/70C07C37/74C07C37/82C07C39/04C07C45/53C07C45/79C07C37/68
    • C07C45/79C07C37/82C07C45/53Y02P20/52Y02P20/584
    • The invention relates to a method for purification of phenol and specifically to a method for purification of phenol produced within the process of joint phenol and acetone production by cumene method.The aim of the invention is to develop a catalyst which has high activity for phenol purification from organic mico-impurities with regeneration of the catalyst and which has high mechanical strength and stability with long catalyst life.This result is obtained by phenol purification using a heterogeneous zeolite catalyst. The acidity of the catalyst measured by butane cracking (K.sub.A) is more than 10.It is preferable to use zeolites which are designated according to the classification of the International Zeolite Association by indices FAU (zeolites X, Y), MFI (for example, ZSM-5), MOR (mordenite), MAZ (omega), BEA (beta), FER (ferrierite) and others. These zeolites can be used with binders (aluminum oxide, silica gel, aluminosilicates or aluminophosphates) and without them. It is preferable to use zeolite of the Y type with an aluminosilicate binder and a the value of K.sub.A =50-80 cm.sup.3 /min*g and Si/Al ratio more than 3. The concentration of sodium, potassium and other alkali agents on the basis of their oxides does not exceed 2 wt %, preferably not more than 0.3 wt %. It is preferable to use zeolites with medium and large pores. Size of zeolites pores should be within the range 4 .ANG. in diameter and more. The most preferable zeolites are with large pores (>6 .ANG. in diameter) such as Y and mordenite.
    • 本发明涉及一种纯化苯酚的方法,特别涉及通过异丙苯法在联苯酚和丙酮生产过程中产生的苯酚纯化方法。 本发明的目的是开发一种催化剂,该催化剂具有较高的活性,用于有机微杂杂质的纯化,催化剂的再生,并具有较高的机械强度和稳定性以及较长的催化剂寿命。 该结果通过使用非均相沸石催化剂的苯酚纯化获得。 通过丁烷裂解(KA)测量的催化剂的酸度大于10.优选使用根据国际沸石协会的分类指定的沸石,通过指数FAU(沸石X,Y),MFI(例如, ZSM-5),MOR(丝光沸石),MAZ(ω),BEA(β),FER(镁碱沸石)等。 这些沸石可以与粘合剂(氧化铝,硅胶,硅铝酸盐或铝磷酸盐)一起使用,没有它们。 优选使用Y型沸石与铝硅酸盐粘合剂,KA = 50-80cm 3 / min * g,Si / Al比大于3。钠,钾和其他碱剂的浓度 其氧化物的基数不超过2重量%,优选不大于0.3重量%。 优选使用具有中孔和大孔的沸石。 沸石孔隙的大小应在直径4 ANGSTROM以内。 最优选的沸石具有大孔(直径大于等于6埃),例如Y和丝光沸石。