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 processing cycle time, secondary pollution of hydrogenated nitrile butadiene rubber, large consumption, etc., to reduce consumption, improve desorption efficiency, The effect of reducing the processing cycle
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Embodiment 1
[0016] The macroporous chelating resin is a copolymer of benzenediene-divinylbenzene with a specific surface area of 500m 2 / g, pore volume is 0.75ml / g, average pore size: 200; particle size distribution: 1~1.5mm (dry basis); bulk density: 880g / l (wet basis), with thiourea group, isosulfide Urea functional group.
[0017] Use the above macroporous chelating resin with thiourea group and isothiourea group to remove the rhodium complex catalyst in HNBR. The specific process is as follows:
[0018] Hydrogenation of 6-25% nitrile rubber in chlorobenzene solution in the presence of rhodium catalyst and triphenylphosphine co-catalyst can obtain HNBR.
[0019] About 10g of macroporous chelating resin with thiourea group and isothiourea group functional group is arranged in an ion exchange column with a length of about 20cm and an inner diameter of about 1.0cm. The ion exchange column is preheated at 60-90°C, and 1000 g of 6% HNBR glue is passed through the ion exchange column at a flo...
Embodiment 2
[0022] Use about 10g of the same macroporous chelating resin of the benzenediene-divinylbenzene copolymer as in Example 1 but with mercapto and isothiourea functional groups to remove the residual rhodium catalyst in the HNBR glue. Process As described in Example 1, the rhodium content in the treated HNBR was 20 ppm, and the rhodium removal rate was 87%.
Embodiment 3
[0024] Use about 10g of the same macroporous chelating resin of benzodiene-divinylbenzene copolymer as in Example 1, but with mixed functional groups of mercapto, thiourea and isothiourea (mercapto: thiourea: isothiourea = 90-98:2-8:0-3). Using it to remove the residual rhodium catalyst in the HNBR glue solution, the process is the same as that described in Example 1. The rhodium content in the treated HNBR is 8 ppm, and the rhodium removal rate is 94.8%.
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