Method for removing residual rhodium catalyst from hydrogenated nitrile rubber
A technology for hydrogenating nitrile butadiene rubber and rhodium catalysts, which is applied in the field of removing residual rhodium catalysts, can solve the problems of long treatment cycle time, large consumption, secondary pollution of hydrogenated nitrile butadiene rubber, etc., and achieves reduced consumption, reduced treatment period, and improved The effect of desorption efficiency
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Embodiment 1
[0016] The macroporous chelating resin is a copolymer of styrene-divinylbenzene, with a specific surface area of 500m 2 / g, pore volume is 0.75ml / g, average pore diameter: 200 Å; particle size distribution: 1~1.5mm (dry basis); bulk density: 880g / l (wet basis), with thiourea group, isosulfur Urea functional group.
[0017] With the above-mentioned thiourea group, the macroporous chelating resin of the isothiourea group functional group removes the rhodium complex catalyst in the HNBR, and the concrete process is as follows:
[0018] In the presence of a rhodium catalyst and a triphenylphosphine co-catalyst, the chlorobenzene solution of 6-25% nitrile rubber is hydrogenated to obtain HNBR.
[0019] Arrange about 10 g of macroporous chelating resin with thiourea group and isothiourea group in an ion exchange column with a length of about 20 cm and an inner diameter of about 1.0 cm. The ion-exchange column is preheated at 60-90°C, and 1000g of 6% HNBR glue is passed through t...
Embodiment 2
[0022] But with the macroporous chelating resin of about 10g same benzenediene-divinylbenzene copolymer as embodiment 1, have mercapto group, isothiourea functional group, remove residual rhodium catalyst in the HNBR glue solution with it, technological process As described in Example 1, the rhodium content in the treated HNBR is 20 ppm, and the removal rate of rhodium is 87%.
Embodiment 3
[0024] With the macroporous chelating resin of about 10g and embodiment 1 identical styrene-divinylbenzene copolymer but have mercapto group, thiourea group, isothiourea mixed functional group (mercapto group: thiourea group: isothiourea= 90-98: 2-8: 0-3). , remove residual rhodium catalyst in the HNBR glue solution with it, technological process is described with embodiment 1, rhodium content is 8ppm in the HNBR after processing, and the removal rate of rhodium is 94.8%.
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Abstract
Description
Claims
Application Information
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