Production system of rubber filler
A production system and filler technology, applied in refining to remove heteroatoms, chemical instruments and methods, chemical/physical processes, etc., can solve problems such as damage to catalyst performance, reduction of catalyst service life, and inability of catalyst to be fully utilized.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2019-10-08
- Estimated Expiration
- Not applicable · inactive patent
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Abstract
Description
technical field
[0001] The invention relates to the technical field of rubber filler production, in particular to a rubber filler production system. Background technique
[0002] As a rubber filler, white oil is more and more widely used in the process of cooperating with rubber. It is an indispensable substance in the rubber industry. The production of white oil is by crude oil normal pressure and vacuum fractionation, solvent extraction and dewaxing. Hydrogenation derived. Hydrofining is an important step in white oil production. By heating the material to a certain temperature and mixing it with hydrogen, the hydrogenation reaction is completed under the action of a catalyst. Hydrofining requires a hydrogenation reactor. The existing hydrogenation The following problems generally exist in the reactor: (1) The hydrogenation process is an exothermic reaction, and the raw material oil is fed from the center of the top of the reactor, and most of them are concentrated in the...
Examples
Embodiment Construction
[0021] In order to better understand the technical content of the present invention, specific embodiments are provided below, and the present invention is further described in conjunction with the accompanying drawings.
[0022] see Figure 1 to Figure 5 , the present invention provides a production system for rubber fillers, including a reaction tank 1, the top of the reaction tank 1 is provided with a feed pipe 2, crude oil and hydrogen are mixed and heated to reach the reaction temperature and then transported through the feed pipe 2 In the reaction tank 1, several catalyst beds 3 are sequentially arranged in the reaction tank 1 from top to bottom. After crude oil enters the reaction tank 1, it passes through each section of the catalyst bed 3, layer by layer. Carry out hydrogenation reaction, the top of described catalyst bed 3 is provided with diverter mechanism 4, and described diverter mechanism 4 is positioned at the bottom of described feed pipe 2, and described diver...