Aq. dispersions of polyolefine fibrids - opt. mixed with cellulose fibres, prepd. by using polyoxyalkylated sulphated alcohol dispersants

    公开(公告)号:DE2528497A1

    公开(公告)日:1977-01-20

    申请号:DE2528497

    申请日:1975-06-26

    Applicant: BASF AG

    Abstract: The dispersions are prepd. by dispersing the fibrous prods in the presence of a dispersant. Dispersant consists of polyoxyalkylated sulphated alcohols contg. 1-6 structural units having formula -C-O- (CH2CH2O)x (CH2CHMeO) SO3M(I) (where x = 0-30; y = 1-35; M = Na, K or NH4+ and Me is methyl). The fibrid dispersions can be processed to paper or textile-like sheets and webs. Used of (I) prevents foaming and agglomeration on distn. of fibrid dispersions and in sheet formation, esp. on paper machines. Fibre-bonding and initial wet-strength of webs obtd. is improved. Small quantities of (I) are sufficient to disperse the hydrophobic fibrids in water. In an example, high density polyethylene fibrids were mixed with sulphite pulp in water. Dispersion was added to a sheet-former contg. water. 1% CH2O 2 - (CH2-CH2O)38(CH2CHMeO)4o (SO3Na)2 was used as dispersant. The sheets obtd. had wt/area 130 g/m2, initial wet strength 70g. Foaming on distn. and sheet-forming was weak. No sheet could be formed in absence of (I).

    Continuous mixing of materials of widely differing viscosity - using screw extruders of special design

    公开(公告)号:DE2551352A1

    公开(公告)日:1977-05-26

    申请号:DE2551352

    申请日:1975-11-15

    Applicant: BASF AG

    Abstract: Continuous prodn. of homogeneous mixts. of (A) a low viscosity component of 1-1000 Ns/m2 viscosity and (B) a high viscosity component with viscosity 102-104 Ns/m2 higher than (A), with (A) being 70-99 wt. % of the total by passing (B) through a screw extruder with L/D ratio 30-60 (40-50) and adding (A) in up to 4 separate stages, in amounts of 30-60, 80-130, 400-550 and 800-1200 wt. % w.r.t. initial amount of (B) at each stage. Used for prepn. of sealants, adhesives, rubber solns. multi-grade lubricating oils, etc. in which (B) is a polymer e.g. synthetic or natural rubber, polyiso-butylene, polyvinyl ether etc. and (A) is oil bitumen, polyisobutylene polyethylene wax, paraffin wax etc. Homogeneous mixts. free from undsipersed high-viscosity material are obtd. in a continuous process, without laborious multi-stage batch mixing using incremental addns. of (A).

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