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System for adjusting hydrogen-carbon ratio of synthesis gas and simultaneously producing byproduct hydrogen through coupling of membrane separation and pressure swing adsorption

A technology of pressure swing adsorption and coupling adjustment, which is applied in hydrogen/synthesis gas production, hydrogen separation, diffusion hydrogen separation, etc., to achieve the effects of reducing operating costs, reducing power consumption, and low energy consumption

Pending Publication Date: 2021-12-03
TIANBANG NAT ENG RES CENT OF MEMBRANE TECH
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  • Claims
  • Application Information

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Problems solved by technology

[0010] In order to solve the problems described in the background technology and overcome the technical defects of a single technology to adjust the hydrogen-to-carbon ratio of syngas while by-producing hydrogen, the present invention provides a coupling process of membrane separation and pressure swing adsorption to adjust the hydrogen-to-carbon ratio of syngas while by-producing hydrogen system

Method used

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  • System for adjusting hydrogen-carbon ratio of synthesis gas and simultaneously producing byproduct hydrogen through coupling of membrane separation and pressure swing adsorption
  • System for adjusting hydrogen-carbon ratio of synthesis gas and simultaneously producing byproduct hydrogen through coupling of membrane separation and pressure swing adsorption
  • System for adjusting hydrogen-carbon ratio of synthesis gas and simultaneously producing byproduct hydrogen through coupling of membrane separation and pressure swing adsorption

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Embodiment 1

[0035] Crude feed gas conditions:

[0036]

[0037] Gas separation requirements:

[0038] Product gas 1: hydrogen for export: flow rate is about 6350Nm 3 / h, purity H2>99.9%, pressure ≥2.4MPaG.

[0039] Product gas 2: Gases other than hydrogen are mixed into "carbonylation synthesis gas", which is used as the raw material for the downstream carbonylation unit. The ratio of H2:CO in this "carbonylation synthesis gas" is required to be about 1:1 (molar ratio). Pressure ≥ 2.3MPaG.

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Abstract

The invention discloses a system for adjusting the hydrogen-carbon ratio of synthesis gas and simultaneously producing a byproduct hydrogen by coupling membrane separation and pressure swing adsorption, wherein raw material gas firstly enters a membrane separator, permeate gas and impermeable gas are obtained under the pushing of the pressure difference of two sides of a separation membrane, the permeate gas is subjected to pressure swing adsorption to purify high-concentration product hydrogen and desorption gas with higher carbon monoxide concentration, the desorption gas is pressurized by a compressor and then is mixed with the membrane separation impermeable gas to form the synthesis gas with the hydrogen-carbon ratio meeting the requirement. The amount of permeate gas entering pressure swing adsorption is adjusted by adjusting the operation pressure of membrane separation or the membrane separation area, so that the hydrogen production amount of pressure swing adsorption is adjusted, and the hydrogen-carbon ratio of the synthesis gas is adjusted. The advantages of two gas separation methods of membrane separation and pressure swing adsorption are fully utilized, the whole set of system is low in energy consumption, no exhaust waste gas is generated, and the purposes of adjusting the hydrogen-carbon ratio of the synthesis gas and producing high-concentration hydrogen as a byproduct are achieved at the same time.

Description

technical field [0001] The invention relates to the field of gas separation in coal chemical industry and petrochemical industry, in particular to a system for adjusting the hydrogen-carbon ratio of synthesis gas and simultaneously producing hydrogen by-product through membrane separation and pressure swing adsorption coupling process. Background technique [0002] The production of different chemical products with syngas requires that the syngas have different hydrogen-to-carbon ratios, such as; Fischer-Tropsch synthesis requires a hydrogen-to-carbon ratio of 3 to 3.6; the synthesis of methanol requires a hydrogen-to-carbon ratio of 2.05 to 2.25; dipropylheptanol (2PH) production requires the hydrogen-to-carbon ratio to be maintained at 1.02 as much as possible; the carbonylation reaction requires a hydrogen-to-carbon ratio of about 1, and the hydrogen-to-nitrogen ratio of synthetic ammonia is required to be 3, so the ratio of synthesis gas is a necessary adjustment method f...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/56
CPCC01B3/56C01B3/501C01B2203/042C01B2203/06
Inventor 何绍辉徐徜徉杨文皓
Owner TIANBANG NAT ENG RES CENT OF MEMBRANE TECH
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