CIESC Journal ›› 2019, Vol. 70 ›› Issue (7): 2528-2539.DOI: 10.11949/0438-1157.20190113
• Catalysis, kinetics and reactors • Previous Articles Next Articles
Yixuan YIN1(),Tingting CHENG2,Xiaojun BAO1,Pei YUAN1()
Received:
2019-02-11
Revised:
2019-04-11
Online:
2019-07-05
Published:
2019-07-05
Contact:
Pei YUAN
通讯作者:
袁珮
作者简介:
阴义轩(1993—),女,硕士研究生,<email>893584980@qq.com</email>
基金资助:
CLC Number:
Yixuan YIN, Tingting CHENG, Xiaojun BAO, Pei YUAN. Deactivation and regeneration of heterogeneous catalysts for hydrogenation of nitrile butadiene rubber[J]. CIESC Journal, 2019, 70(7): 2528-2539.
阴义轩, 成婷婷, 鲍晓军, 袁珮. 丁腈橡胶非均相加氢催化剂失活原因及再生性能研究[J]. 化工学报, 2019, 70(7): 2528-2539.
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波数/cm-1 | 基团种类 | 吸收因子 | 峰强度变化 |
---|---|---|---|
3500 | —NH2 或 —NH— | — | —CN被加氢还原后新出现的峰 |
2236 | —CN | 1.0 | 此为内标计算加氢度 |
970 | 1,4-trans unit, —CH=CH— | 2.3 | 加氢度增加,峰强度减弱或消失 |
920 | 1,2 unit, —CH=CH2 | 2.24 | 加氢度增加,峰强度减弱或消失 |
750 | 1,4-cis unit, —CH=CH— | 0.36 | 加氢度增加,峰强度减弱或消失 |
723 | —[CH2] n — (n?4) | 0.25 | C=C被加氢还原,出现亚甲基的特征峰 |
Table 1 Characteristic peaks for NBR and HNBR FT-IR spectra [33]
波数/cm-1 | 基团种类 | 吸收因子 | 峰强度变化 |
---|---|---|---|
3500 | —NH2 或 —NH— | — | —CN被加氢还原后新出现的峰 |
2236 | —CN | 1.0 | 此为内标计算加氢度 |
970 | 1,4-trans unit, —CH=CH— | 2.3 | 加氢度增加,峰强度减弱或消失 |
920 | 1,2 unit, —CH=CH2 | 2.24 | 加氢度增加,峰强度减弱或消失 |
750 | 1,4-cis unit, —CH=CH— | 0.36 | 加氢度增加,峰强度减弱或消失 |
723 | —[CH2] n — (n?4) | 0.25 | C=C被加氢还原,出现亚甲基的特征峰 |
样品 | 结构类型 | H种类 | 化学位移 |
---|---|---|---|
NBR | 1,4 单元 | —CH=CH— | 5.50 |
—CH2— | 2.15 | ||
—CH(CN) — | 2.65 | ||
—CH2CH(CN) — | 1.70 | ||
1,2 单元 | =CH—和=CH2 | 4.90—5.10 | |
HNBR | —CH3 | 0.90 | |
—CH2— | 1.30 | ||
—CH(CN) — | 2.60 | ||
—CH2—CH(CN) — | 1.50 |
Table 2 Chemical shifts of H protons in different microstructures of NBR or HNBR [33]
样品 | 结构类型 | H种类 | 化学位移 |
---|---|---|---|
NBR | 1,4 单元 | —CH=CH— | 5.50 |
—CH2— | 2.15 | ||
—CH(CN) — | 2.65 | ||
—CH2CH(CN) — | 1.70 | ||
1,2 单元 | =CH—和=CH2 | 4.90—5.10 | |
HNBR | —CH3 | 0.90 | |
—CH2— | 1.30 | ||
—CH(CN) — | 2.60 | ||
—CH2—CH(CN) — | 1.50 |
Fig. 4 N2 adsorption-desorption isotherms and pore diameter distribution curves obtained from adsorption branches of catalyst before and after reaction
催化剂 | 比表面积/(m2/g) | 孔容/(cm3/g) | 平均孔径/nm |
---|---|---|---|
反应前 | 494 | 1.55 | 12.5 |
反应后 | 281 | 0.87 | 12.3 |
Table 3 Physical properties of catalyst before and after reaction
催化剂 | 比表面积/(m2/g) | 孔容/(cm3/g) | 平均孔径/nm |
---|---|---|---|
反应前 | 494 | 1.55 | 12.5 |
反应后 | 281 | 0.87 | 12.3 |
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