Method for removing sulfur oxide and nitrogen oxide in catalytic cracking regenerated smoke

A technology for catalytic cracking and flue gas regeneration, applied in the direction of catalyst regeneration/reactivation, chemical instruments and methods, separation methods, etc., can solve the problems of treatment technology, flue gas and dry gas that have not yet been seen, and simplify the process Effect

Active Publication Date: 2014-12-31
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
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  • Claims
  • Application Information

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Problems solved by technology

From the existing technologies, the removal of sulfur oxides in flue gas and hydrogen sulfide in dry gas is carried out separately, and there is no report on the technology of treating flue gas and dry gas together.

Method used

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  • Method for removing sulfur oxide and nitrogen oxide in catalytic cracking regenerated smoke

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Embodiment Construction

[0020] The method for removing sulfur oxides and nitrogen oxides in catalytic cracking regenerated flue gas provided by the invention is implemented in this way:

[0021] The heavy hydrocarbon oil raw material is introduced into the catalytic cracking reactor, and is contacted and reacted with the hot regenerated catalytic cracking catalyst. After the gas-solid separation of the generated reaction oil gas and the catalyst, the reaction oil gas is introduced into the fractionation tower of the catalytic cracking unit for fractionation to obtain dry gas and liquefaction. Gas, gasoline, diesel and other distillates. The carbon-deposited catalyst is stripped and introduced into the regenerator, and the bottom of the catalytic cracking regenerator is introduced with oxygen-containing gas, and the catalyst is reacted with the oxygen-containing gas to burn off the carbon deposit on the catalyst to obtain the regenerated catalyst and regenerated flue gas. ; The regenerated catalyst is...

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Abstract

A method for removing sulfur oxide and nitrogen oxide in catalytic cracking regenerated smoke comprises the steps of injecting a reduction gas flow in the middle-upper part of a catalytic cracking regenerator, enabling regenerated smoke at the upper part of the regenerator to be contacted with the reduction gas and catalyst particles, conducting redox reaction on sulfur oxide, nitrogen oxide as well as oxygen in the smoke and hydrogen sulfide, hydrogen as well as small-molecular hydrocarbon in the reduction gas flow to generate gas elemental sulfur, nitrogen and steam; and enabling the mixed smoke containing gas sulfur after the reaction to enter a energy recycling system, arranging a liquid sulfur and solid sulfur collector at the low-temperature position to recycle the elemental sulfur, and discharging the catalytic cracking regenerated smoke reaching the standard. According to the method provided by the invention, the subsequent desulfuration treatment process of the smoke containing sulfur in a catalytic cracking device can be saved, so that the pollutant treatment process of the catalytic cracking device can be simplified, and the strong guaranteeing can be provided for the cleaning production of the catalytic cracking device.

Description

technical field [0001] The present invention relates to a method for waste gas treatment, more specifically, relates to a method for removing sulfur oxides and / or nitrogen oxides from regenerated flue gas discharged from a regenerator in a catalytic cracking unit, and recovering elemental sulfur. Background technique [0002] The catalytic cracking catalyst is circulated between the reactor and the regenerator. Usually, when leaving the reactor, the catalyst contains about 3-10wt% coke, and the deposited coke must be burned with oxygen in the air in the regenerator to restore catalytic activity. . The coke deposited on the catalyst is mainly a reaction condensate, and its main components are carbon and hydrogen. When the cracking raw material contains sulfur and nitrogen, the coke also contains sulfur and nitrogen. The carbon-deposited catalyst is regenerated with oxygen to generate CO 2 , CO and H 2 O, regeneration flue gas also contains SOx (SO 2 , SO 3 ) and NOx (NO,...

Claims

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Application Information

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Patent Type & AuthorityPatents(China)
IPC IPC(8): B01D53/76B01D53/60B01J38/12
CPCY02A50/20
Inventor郭大为张久顺毛安国谢朝钢傅军王巍
OwnerCHINA PETROLEUM & CHEM CORP