Process for preparing substitute natural gas from synthesis gas

A technology for substituting natural gas and synthetic gas, which is applied in the petroleum industry, gas fuel, fuel, etc., and can solve the problems that the high-temperature waste heat of the process gas cannot be well utilized, the cost is high, and the process flow setting is not reasonable.

Active Publication Date: 2012-07-18
CHINA PETROLEUM & CHEM CORP +2
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  • Abstract
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  • Application Information

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Problems solved by technology

The former puts the superheater behind, resulting in insufficient steam superheat, or can only produce superheated medium-pressure steam by-product, resulting in the high-temperature waste heat of the process gas cannot be well utilized, a

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  • Process for preparing substitute natural gas from synthesis gas
  • Process for preparing substitute natural gas from synthesis gas
  • Process for preparing substitute natural gas from synthesis gas

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Embodiment Construction

[0039] The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments.

[0040] Such as Figure 2 to Figure 7 As shown, the structure of the first methanation reactor 1, the steam superheater 2 and the first waste pot 3 used in the process for producing natural gas from synthetic gas is as follows:

[0041] The first methanation reactor 1 mainly includes two parts, namely a catalyst layer 11 and a gas collector 12 arranged below the catalyst layer 11 . The methanation reactor in this embodiment is a vertical cylindrical container, the shell wall is covered with refractory and heat-insulating lining, and the middle part is filled with catalyst. The process gas enters from the top and enters the gas collector 12 at the bottom and then enters the conduit 13 after being reacted by the catalyst. The structure of the methane reactor involved in the present invention belongs to the prior art. The conduit 13 is a water-c...

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Abstract

The invention relates to a process for preparing substitute natural gas from synthesis gas, which comprises the following steps that: after being subjected to detoxification and desulfuration, the raw materials are subjected to heat exchange and are mixed with recycle gas from a third methanator and the obtained mixture is divided into two strands, wherein the first strand enters a first methanator to be subjected to the methanation reaction; all high-temperature first synthesis gas obtained after the first strand of raw material gas reacts in the first methanator is sequentially fed into a steam superheater and a first waste heat boiler to be subjected to heat exchange and then is fed into a second methanator to be subjected to the further methanation reaction to obtain second synthesis gas; after being subjected to heat exchange, the second synthesis gas is mixed with the second strand of raw material gas, and then the mixture is fed into the third methanator; and third synthesis gas discharged out of the third methanator is divided into two strands after being subjected to heat exchange compression, one strand of the third synthesis gas serving as the recycle gas is mixed with the raw material gas, the rest of the third synthesis gas enters a fourth methanator to enable the unreacted raw material gas to be synthesized into methane so as to obtain the synthesis gas capable of replacing the natural gas. The process has the characteristics that the reaction temperature rise is easy to control; the utilization of system energy is optimized; and the like.

Description

technical field [0001] The invention relates to a chemical process, in particular to a process for producing substitute natural gas from synthetic gas. Background technique [0002] The development of high-temperature methanation technology can be traced back to the 1970s. Due to the oil crisis, the United States, Britain and other countries began to study the application of alternative energy sources, including the technology research and development of coal-based high calorific value city gas and alternative natural gas. In 1984, the world's first and only commercial coal-to-natural gas plant put into operation was built. In 1978, a Danish company also built a 7200m 3 / d's synthetic natural gas pilot plant, which has been tested for 3 years. In addition, there are many plants in Europe that use similar technology to produce city gas. Since the 1980s, my country has started the research on gas methanation, but it is mainly the partial methanation of water gas to produce ...

Claims

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Application Information

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IPC IPC(8): C10L3/08
Inventor 杨宏泉刘芹邢涛张骏弛陈央陆亚东李忠燕胡晓昕
Owner CHINA PETROLEUM & CHEM CORP
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