Coupling equipment for realizing temperature adjustment and stripping of catalytic cracking regenerant
A technology of catalytic cracking and coupled equipment, applied in catalytic cracking, cracking, petroleum industry, etc., can solve the problems of large amount of stripping steam, complex stripper structure, high energy consumption, etc., to improve heat extraction and heat exchange efficiency, Effect of suppressing deactivation effect and enhancing heat transfer efficiency
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[0042] Example one
[0043] figure 1 A schematic diagram of a coupling device that can realize temperature adjustment and stripping of a catalytic cracking regenerator is provided. As shown in the figure, the regenerant temperature regulating and stripping coupling device includes a two-stage structure, the upper part is the regenerant temperature regulating section 5, and the lower part is the regenerant stripping section or flue gas degassing section 2. The temperature adjustment section 5 has a cylindrical body in which a number of heat-taking tubes 4 are provided as heat exchange components. The upper part of the cylindrical body is respectively provided with a regenerant inlet 20 and a mixed gas outlet 30. The specific form of the heat pipe 4 can be a commonly used vertical finned tube, a squirrel-cage heat exchange tube or a nail-head heat exchange tube, etc., and you can refer to the description and drawings in the aforementioned Chinese patents 200410083890.3 and 20041008...
Example Embodiment
[0048] Example two
[0049] See figure 2 The difference between the scheme of this embodiment and the first embodiment is that a section of annular flow isolation sleeve 8 is provided in the upper temperature control section 5 of the regenerant temperature control and stripping coupling device, which divides the cross section of the temperature control section 5 into a central flow area (Inner ring area) and outer ring circulation area, image 3 It is a schematic diagram of the cross-sectional structure along the A-direction. The heat pipe is arranged along the wall of the spacer sleeve. The area ratio of the central flow area I and the outer ring flow area II can be 0.5-2. Such as figure 2 As shown, two air distributors are provided at the bottom of the temperature adjustment section 5 to provide fluidized air for the central ring and the outer ring respectively. The central area air distributor 6 can be an annular tube type distributor or a plate type distributor (a plate typ...
Example Embodiment
[0052] Example three
[0053] Refer to the scheme of this embodiment Figure 4 , The difference from the second embodiment is that two annular spacer sleeves 9 and 10 are arranged in the upper temperature regulating section 5 of the regenerant temperature regulating and stripping coupling device. The two stages of spacer sleeves are along the temperature regulating section. The axial direction is set up and down (see section structure image 3 ), leave an appropriate gap d between them, and make the gap 0.1 to 1.0 times the diameter 9 and 10 of the spacer sleeve. Other parameter settings and work flow can be the same as the second embodiment.
[0054] Experimental research shows that the use of two-stage spacer sleeve design has a better effect on improving the heat transfer efficiency of the temperature adjustment section.
[0055] Similarly, this embodiment can also be changed to a three-stage or more-stage flow isolation sleeve structure.
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