A mass transfer enhanced alkylation reactor and alkylation process method
An alkylation reactor and reactor technology, applied in chemical instruments and methods, chemical/physical/physical chemical mobile reactors, organic chemistry, etc., can solve the problems of increasing side reactions and unsuitable heat release, etc., to achieve Reduction of side reactions, good reaction effect, and effect of increasing octane number
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2016-08-17
Smart Images
Figure 1 Figure 2 Figure 3
Abstract
Description
technical field
[0001] The invention relates to an alkylation reactor and an alkylation reaction method, in particular to an alkylation reactor and an alkylation reaction method which adopt isobutane and C3-C5 olefins to catalyze the alkylation reaction. Background technique
[0002] With the development of the economy, especially the rapid development of the transportation industry, the emission of vehicle exhaust is one of the main sources of air pollution. Improving the quality of gasoline is the most important way to reduce the pollution of vehicle exhaust. The alkylated oil obtained by the alkylation reaction of isobutane and C3-C5 olefins has the characteristics of no sulfur, high octane number, small difference between the octane number of the research method and the octane number of the motor method, and is a high-quality An important blending component of clean gasoline.
[0003] Alkylation reaction is a traditional technology in the field of petroleum refining, ma...
Examples
Embodiment 1~3
[0039] use as figure 1 In the reactor with the structure shown, the bed of the rotating bed is made of stainless steel mesh packing, the bed porosity of the stainless steel mesh packing is 0.95, and the specific surface area is 4000m 2 / m 3 , the wire diameter is 1mm, and the volume of the rotating bed accounts for 65% of the total volume of the rotating bed reactor. The alkylation reaction is carried out using concentrated sulfuric acid with a mass concentration of 95% as a catalyst and isobutane and butene as raw materials. The number of annular fin assemblies is set to be 10, and the gap distance between the fin assemblies and the rotating bed is 50mm.
[0040] The molar ratio of isobutane to butene is 1:1-300:1, preferably 3:1-50:1. The volume ratio of acid to hydrocarbon is 0.1:1~5:1, preferably 0.5:1~1.5:1. The reaction temperature is -20-15°C, preferably -10-10°C, most preferably -5-5°C. The reaction pressure is 0.2~1.5MPa, preferably 0.3~0.8MPa. The rotational sp...