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Spray nozzle for catalytic cracking lift pipe and application

A catalytic cracking and riser technology, applied in catalytic cracking, cracking, petroleum industry and other directions, can solve the problem of inability to simulate the spray contact and reaction of heavy diesel oil, and achieve the effects of simple structure, uniform contact and convenient use.

Active Publication Date: 2019-02-26
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the catalytic cracking riser test device simulates the blending of heavy diesel oil in industrial catalytic cracking units, because the existing feed nozzle can only spray out one kind of catalytic cracking raw material, it is impossible to simulate the contact and reaction of heavy diesel oil with the catalyst

Method used

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  • Spray nozzle for catalytic cracking lift pipe and application
  • Spray nozzle for catalytic cracking lift pipe and application
  • Spray nozzle for catalytic cracking lift pipe and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0062] There are 4 hydrocarbon oil I outer spray holes 35 on the hydrocarbon oil I outer spray head 1 described in Example 1, which are evenly arranged on the hydrocarbon oil I outer spray head 1, and the diameter of each spray hole is 0.7 mm.

[0063] One hydrocarbon oil I inner spray hole 36 is provided on the hydrocarbon oil I inner spray head 4 described in Example 1, and the diameter of the spray hole on the hydrocarbon oil I inner spray head 4 is 1.1 mm.

[0064] Four hydrocarbon oil II nozzle holes 37 on the hydrocarbon oil II nozzle 7 described in Example 1 are arranged evenly on the hydrocarbon oil II nozzle 7, and the diameter of each nozzle hole is 1.0 mm.

[0065] The distance D between the hydrocarbon oil I inner spray head 4 and the hydrocarbon oil I outer spray head 1 described in Example 1 is 3 mm.

[0066] The reduced diameter d of the steam chamber 5 described in Example 1 is 4.5mm.

[0067] The ratio of the distance L between the hydrocarbon oil II nozzle 7...

Embodiment 2

[0077] There are two hydrocarbon oil I outer spray holes 35 on the hydrocarbon oil I outer spray head 1 described in Example 2, which are evenly arranged on the hydrocarbon oil I outer spray head 1, and the diameter of each spray hole is 1.1 mm.

[0078] One hydrocarbon oil I inner spray hole 36 is provided on the hydrocarbon oil I inner spray head 4 described in Example 2, and the diameter of the spray hole on the hydrocarbon oil I inner spray head 4 is 1.2 mm.

[0079] Four hydrocarbon oil II nozzle holes 37 on the hydrocarbon oil II nozzle 7 described in Example 2 are arranged evenly on the hydrocarbon oil II nozzle 7, and the diameter of each nozzle hole is 1.1 mm.

[0080] The distance D between the hydrocarbon oil I inner spray head 4 and the hydrocarbon oil I outer spray head 1 described in Example 2 is 3.5 mm.

[0081] The reduced diameter d of the steam chamber 5 described in Example 2 is 4.6 mm.

[0082] The ratio of the distance L between the hydrocarbon oil II nozzl...

Embodiment 3

[0092] One hydrocarbon oil I outer spray hole 35 on the hydrocarbon oil I outer spray head 1 described in Example 3 is arranged uniformly on the hydrocarbon oil I outer spray head 1, and the diameter of each spray hole is 2mm.

[0093] One hydrocarbon oil I inner spray hole 36 is provided on the hydrocarbon oil I inner spray head 4 described in Example 3, and the diameter of the spray hole on the hydrocarbon oil I inner spray head 4 is 1.3 mm.

[0094] Six hydrocarbon oil II injection holes 37 on the hydrocarbon oil II nozzle 7 described in Example 3 are arranged evenly on the hydrocarbon oil II nozzle 7, and the diameter of each injection hole is 0.9mm.

[0095] The distance D between the hydrocarbon oil I inner spray head 4 and the hydrocarbon oil I outer spray head 1 described in Example 3 is 4mm.

[0096] The reduced diameter d of the steam chamber 5 described in Example 3 is 4.7mm.

[0097] The ratio of the distance L between the hydrocarbon oil II nozzle 7 and the hydro...

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PUM

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Abstract

The invention relates to a spray nozzle for a catalytic cracking lift pipe and an application. The spray nozzle can simultaneously spray two raw materials and comprises a hydrocarbon oil I outer sleeve pipe, a hydrocarbon oil I inner sleeve pipe, a hydrocarbon oil I outer spray head, a hydrocarbon oil I inner spray head, a steam chamber, a hydrocarbon oil I and steam mixing chamber, a hydrocarbonoil II spray head and a hydrocarbon oil II circular atomizing chamber. The spray nozzle can be applied to a catalytic cracking lift pipe device which successively comprises a light hydrocarbon reaction zone I, a heavy hydrocarbon reaction zone and a light hydrocarbon reaction zone II from bottom to top along the vertical direction of a lift pipe reactor. According to the invention, through arrangement of the hydrocarbon oil II circular atomizing chamber on the spray nozzle, the spray nozzle provided by the invention can simultaneously spray two raw materials, and can be used for the catalyticcracking lift pipe experimental device for experimental study of simultaneous contact and reaction of different catalytic raw materials with a catalyst; and light hydrocarbons sprayed by the hydrocarbon oil II spray head preferentially contact with the catalyst for a reaction to generate a large amount of carbonium ions, so conversion of heavy hydrocarbons is accelerated, and the spray nozzle provided by the invention has the characteristic of reducing the diesel-to-gasoline ratio of catalytic cracking.

Description

technical field [0001] The invention relates to a catalytic cracking conversion device for petroleum hydrocarbons, in particular to a catalytic cracking riser feed nozzle and its application. Background technique [0002] As the main light oil production process in the oil refining industry, catalytic cracking has attracted extensive attention from major research and development institutions at home and abroad because of its wide applicability and relatively low processing cost. Catalytic cracking provides 75% of gasoline components in my country's commercial gasoline pool, and plays a pivotal role in refineries. In the catalytic cracking process and catalyst research and development process, the catalytic cracking riser test device is used in the screening of catalytic cracking catalyst formula, the cracking performance of catalytic raw materials and the investigation of product properties, the evaluation of catalytic cracking catalyst, the optimization and simulation of in...

Claims

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Application Information

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IPC IPC(8): C10G11/18
CPCC10G11/18
Inventor 侯凯军高永福王智峰高雄厚张海涛张忠东李荻孟凡芳孙书红张爱萍柳召永樊红超苏怡
Owner PETROCHINA CO LTD
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