Micro-interface reaction system and method for petroleum resin hydrogenation
An interfacial reaction, petroleum resin technology, applied in the fields of mixing methods, petroleum industry, hydrotreating process, etc., can solve the problems of decreased intrinsic safety, high reaction pressure of trickle bed hydrogenation process, high equipment investment cost, and high operating cost , to achieve the effect of improving the dispersion and crushing effect, good product quality and low reaction temperature
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2020-12-01
- Estimated Expiration
- Not applicable · inactive patent
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Figure 1
Abstract
Description
technical field
[0001] The invention relates to the field of petroleum resin hydrogenation, in particular to a micro-interface reaction system and method for petroleum resin hydrogenation. Background technique
[0002] Petroleum resin is an important basic chemical raw material and one of the important organic chemical products that has developed rapidly in recent years. Since C9 petroleum resin contains high unsaturated bonds, it is easy to react under the action of oxygen and other chemical substances, which greatly limits the application of petroleum resin, so it is necessary to carry out hydrogenation treatment on petroleum resin.
[0003] The relative molecular weight of C9 petroleum resin (200-3000) is relatively large. Usually, under the catalysis of high-activity catalysts, the operating conditions reach 10-20MPa and 230-300°C to achieve better hydrogenation effect. In addition, there are toxic impurities such as sulfur and nitrogen in C9 petroleum resin, and the ca...
Examples
Embodiment
[0056] refer to figure 1 As shown, it is a micro-interface reaction system for petroleum resin hydrogenation according to an embodiment of the present invention, which mainly includes a pre-hydrogenation reactor 100 and a refining hydrogenation reactor 120;
[0057] The pre-hydrogenation reactor 100 is a fixed-bed reactor, and two catalyst beds are arranged inside it, and a micro-interface generator 140 is arranged between the catalyst bed and the bottom of the pre-hydrogenation reactor 100. The micro-interface generator 140 is two, and two catalyst beds are arranged in the refining hydrogenation reactor 120, and a micro-interface generator 140 is respectively arranged between the two catalyst beds and the bottom of the refining hydrogenation reactor 120 , the number of micro-interface generators 140 set inside the refining hydrogenation reactor 120 is the same as the number of micro-interface generators set inside the pre-hydrogenation reactor 100, both being two.
[0058] T...