Riser catalysis device for processing heavy oil and application thereof
A riser and heavy oil technology, applied in catalytic cracking, chemical instruments and methods, cracking, etc., can solve problems such as insufficient reaction depth, achieve the effects of overcoming insufficient reaction depth, avoiding vicious adsorption competition, and reducing temperature
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2013-11-06
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Abstract
Description
technical field
[0001] The invention relates to a catalytic device and application of petroleum hydrocarbons under non-hydrogen-facing conditions, more specifically, a riser catalytic cracking device for processing low-quality heavy oil and its application. Background technique
[0002] In order to strengthen the catalytic reaction in the reaction process, reduce thermal cracking reaction and unfavorable secondary reaction, the representative process technology is the two-stage riser catalytic cracking technology disclosed by CN1118539C, CN1262625C, etc., which is characterized by two-stage riser reaction Catalysts are used in series and relay mode to achieve the purpose of oil-gas series connection, catalyst relay, staged reaction, shortening reaction time and improving the average performance of catalysts. When this type of technology processes wax oil with better raw material properties, the yield of light oil is higher, especially the yield of diesel oil and cetane numbe...
Examples
Embodiment Construction
[0026] The riser catalytic device for processing heavy oil according to the present invention is composed of a main riser reactor, an auxiliary riser reactor, a gas-solid separation system and a regeneration device; the main riser reactor is located next to the regeneration device and is a variable-diameter lift The middle part of the main riser reactor is a diameter-expanding riser 7, and the upper riser 15 of the main riser is an outlet section whose radial direction is equal to or reduced in the radial direction of the lower riser of the main riser, and is connected with the gas-solid separation system The settler 9 of the main riser is connected, and the lower riser 5 is provided with a lifting steam inlet a1, an inferior heavy oil inlet 3, and a regeneration inclined pipe a16. The height of the pipe 7 accounts for 20-75% of the height of the main riser, and the ratio of the diameter of the expanded diameter riser 7 to the lower riser of the main riser is (1.0-3.0): 1;
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