Process for preparing aromatic iodine compounds
一种芳族化合物、化合物的技术,应用在制备碘化芳族化合物领域,能够解决无法充分提高反应物进料流量、二碘代化合物产率下降等问题,达到稳定控制、稳定反应温度、延长使用周期的效果
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Embodiment 1
[0072] use as figure 2 The equipment shown, with the same conditions of comparative example 1, add benzene (102.4g / hr), iodine (66.9g / hr) and one iodobenzene (483.8g / hr) in the presence of Na-13X zeolite catalyst to carry out iodine reaction. In addition, diiodobenzene (65.9 g / hr) was also added, based on the total feed material (Feed), wherein the composition of diiodobenzene was 9% (wt%). At this time, the molar ratio of non-halogenated aromatic compound / iodine added was 1.93. The diiodobenzene used in this paper is not a single material, but a liquid diiodobenzene obtained by crystallization and solid / liquid separation of the three isomers (para, ortho, meta) of diiodobenzene Mixture (para, ortho, meta).
[0073] also, Figure 4 Shown is a temperature profile according to the length of the reactor measured at the center of the reactor in the same manner as in Comparative Example 1. Table 1 shows the reaction conditions and the data of the reaction products.
[0074] In...
Embodiment 2
[0076] use as figure 2 The equipment shown, with the same conditions of comparative example 1, add benzene (98.1g / hr), iodine (47.8g / hr) and one iodobenzene (458.7g / hr) in the presence of Na-13X zeolite catalyst to carry out iodine reaction. In addition, diiodobenzene (115.1 g / hr) was added, based on the total feed material (Feed), wherein the composition of diiodobenzene was 16% (wt%). At this time, the molar ratio of non-halogenated aromatic compound / iodine added was 1.93.
[0077] also, Figure 4 Shown is a temperature profile according to the length of the reactor measured at the center of the reactor in the same manner as in Comparative Example 1. Table 1 shows the reaction conditions and the data of the reaction products.
[0078] In particular, all regions of the reactor are maintained at a nearly constant temperature. The temperature in the upper part of the reactor is maintained below about 300°C, which is close to the desired temperature. The reaction temperat...
Embodiment 3
[0080] use as figure 2 The equipment shown, with the same conditions of comparative example 1, add benzene (91.3g / hr), iodine (47.87g / hr) and one iodobenzene (422.7g / hr) in the presence of Na-13X zeolite catalyst to carry out iodine reaction. In addition, diiodobenzene (162.2 g / hr) was added, based on the total feed material (Feed), wherein the composition of diiodobenzene was 22% (wt%). At this time, the molar ratio of non-halogenated aromatic compound / iodine added was 1.93.
[0081] also, Figure 4 Shown is a temperature profile according to the length of the reactor measured at the center of the reactor in the same manner as in Comparative Example 1. Table 1 shows the reaction conditions and the data of the reaction products.
[0082] In particular, all regions of the reactor are maintained at a nearly constant temperature. The temperature in the upper part of the reactor is maintained below about 300°C, which is close to the desired temperature. The reaction tempera...
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