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Circulating CO shift process of saturation tower

A process and gas shift technology, applied in the field of CO shift process, can solve the problems of short catalyst life, easy over-temperature, high energy consumption, and achieve the effects of long stable operation period, mild operating environment and reduced steam consumption.

Active Publication Date: 2015-05-13
SINOPEC NINGBO ENG +2
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] The technical problem to be solved by the present invention is to provide a saturated tower circulating CO shift process in view of the current state of the art, so as to solve a series of problems such as easy overheating of the shift furnace in the existing high water-gas ratio CO shift process, short catalyst life, and high energy consumption. technical problem

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  • Circulating CO shift process of saturation tower
  • Circulating CO shift process of saturation tower

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Embodiment

[0026] This embodiment is used in conjunction with a typical fertilizer plant that produces 300,000 tons / year of synthetic ammonia and 520,000 tons / year of urea through gasification of Shell pulverized coal gasification.

[0027] like figure 1 As shown, the saturated tower cycle CO shift process includes the following steps:

[0028] The crude oil sent from the pulverized coal gasification unit has a temperature of 155°C to 165°C, a pressure of 3.65Mpa (G) to 3.75Mpa (G), a water / dry gas molar ratio of 0.18 to 0.19, and a CO dry basis volume content of 60% to 70%. The synthesis gas is divided into two streams, the volume ratio of the first stream of crude synthesis gas to the second stream of crude synthesis gas is 70-80:30-20;

[0029] The first stream of crude synthesis gas enters the saturation tower 1 from the lower part of the side wall of the saturation tower, and contacts with the process circulating water with a temperature of 205°C to 215°C sent from the bottom of th...

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Abstract

The invention relates to a circulating CO shift process of a saturation tower. The circulating CO shift process comprises the following steps that a coarse synthetic gas from a pulverized coal gasification unit is divided into two branches, the first branch of coarse synthetic gas is moisturized and heated in the saturation tower and then mixed with high pressure steam and a first branch of primary shift gas and replenished with medium-pressure boiler water, and then the obtained mixture is fed into a No.1 shift furnace for shift reaction, the obtained primary shift gas is divided into two branches after heat exchange, the second branch of primary shift gas is mixed with the first branch of coarse synthetic gas to obtain a primary shift mixed gas, the primary shift mixed gas is mixed and replenished with medium-pressure steam and then fed into a No.2 shift furnace for continuous shift reaction, and the secondary shift gas is fed into a No.3 shift furnace for reaction after heat exchange. The operation of dividing the coarse synthetic gas and the primary shift gas into branches in the circulating CO shift process, so that the CO concentration entering the shift furnaces is effectively reduced; the operating temperatures of the shift furnaces are low, and the operating environment of a catalyst is mild, so that the service life of the catalyst and the operation period of the device are prolonged; and meanwhile, the amount of steam used is reduced, and the effects of energy conservation and consumption reduction are remarkable.

Description

technical field [0001] The invention relates to a CO conversion process, in particular to a saturated tower circulation CO conversion process. Background technique [0002] In recent years, my country's coal gasification technology has made great progress, especially the pulverized coal pressurized gasification technology using waste heat boiler process, which has the characteristics of low coal quality requirements, high effective components in syngas, low operating costs and environmental friendliness. It is adopted by more and more large coal chemical plants in China. The crude synthesis gas produced by pulverized coal pressurized gasification technology in the waste heat boiler process usually has a CO dry basis volume content of more than 60% and a water vapor volume content of less than 20%. The crude synthesis gas has a significant low water vapor content and a high CO content. features. [0003] When the pulverized coal pressurized gasification technology in the was...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10K3/04
CPCY02P20/10
Inventor 施程亮许仁春程雄志曹立群张俊方啸杨玉才
Owner SINOPEC NINGBO ENG
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