Sulfur tolerant catalyzing process for preparing low carbon alcohol from synthesis gas and co-producing natural gas

A low-carbon alcohol and synthesis gas technology, applied in the preparation of hydroxyl compounds, organic compounds, petroleum industry, etc., to achieve the effects of increased production costs, good industrial prospects, and improved carbon utilization

Active Publication Date: 2010-06-16
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
View PDF8 Cites 22 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

After searching, no method was found to produce low-carbon alcohol and co-p

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Sulfur tolerant catalyzing process for preparing low carbon alcohol from synthesis gas and co-producing natural gas
  • Sulfur tolerant catalyzing process for preparing low carbon alcohol from synthesis gas and co-producing natural gas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] This embodiment adopts figure 1 The process flow shown. Coal-based synthesis gas (with a hydrogen-to-carbon molar ratio of 2) enters the crude desulfurization unit and adopts the tannin extraction method for crude desulfurization to obtain a synthesis gas with a sulfur content of less than 100ppm. After mixing with the tail gas recycled to the synthesis reaction of low-carbon alcohols, it enters the synthesis of low-carbon alcohols Device, at a reaction temperature of 300°C, a reaction pressure of 6MPa, and a space velocity of 3000h -1 (V / V), DOW Corporation MoS 2 -React under the action of M-K catalyst, the product enters the condensing device through the pipeline, and condenses at a temperature of 0°C and a pressure of 6MPa to obtain the liquid phase of alcohol, water and oil, CO, H 2 , CO 2 、C 1 -C 5 Exhaust gas mixture composed of hydrocarbons. The alcohol-water-oil liquid phase is mixed with the alcohol-water-oil liquid phase obtained by the condensation of t...

Embodiment 2

[0033] This embodiment adopts figure 1 The process flow shown. Coal-based synthesis gas (hydrogen-to-carbon molar ratio is 1.5) enters the crude desulfurization unit and uses the ADA method for crude desulfurization to obtain a synthesis gas with a sulfur content of less than 100ppm. After mixing with the tail gas recycled to the synthesis reaction of low-carbon alcohols, it enters the low-carbon alcohol synthesis unit , at a reaction temperature of 320°C, a reaction pressure of 8MPa, and a space velocity of 5000h -1 (V / V), DOW Corporation MoS 2 -Reaction under the action of M-K catalyst, the product enters the condensing device through the pipeline, and condenses at a temperature of 4°C and a pressure of 8MPa to obtain the liquid phase of alcohol, water and oil, CO, H 2 , CO 2 、C 1 -C 5 Exhaust gas mixture composed of hydrocarbons. The alcohol-water-oil liquid phase is mixed with the alcohol-water-oil liquid phase obtained by the condensation of the methanation reaction...

Embodiment 3

[0035] This embodiment adopts figure 1 The process flow shown. Coal-based synthesis gas (hydrogen-to-carbon molar ratio is 1) enters the crude desulfurization unit and uses the MSQ method for rough desulfurization to obtain synthesis gas with a sulfur content of less than 100ppm. After mixing with the tail gas recycled to the synthesis reaction of low-carbon alcohols, it enters the low-carbon alcohol synthesis unit. At a reaction temperature of 340°C, a reaction pressure of 10MPa, and a space velocity of 6000h -1 (V / V), DOW Corporation MoS 2 -Reaction under the action of M-K catalyst, the product enters the condensing device through the pipeline, and condenses at a temperature of 5°C and a pressure of 10MPa to obtain the liquid phase of alcohol, water and oil, CO, H 2 , CO 2 、C 1 -C 5 Exhaust gas mixture composed of hydrocarbons. The liquid phase of alcohol water oil is mixed with the alcohol water oil liquid phase obtained by condensation of the methanation reaction pro...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to a sulfur tolerant catalyzing process for preparing low carbon alcohol from synthesis gas and co-producing natural gas, which comprises the following steps: performing a synthetic reaction by contacting the synthesis gas with a sulfur tolerant low carbon alcohol synthetic catalyst after the synthesis gas is subjected to coarse desulphurization; condensing the synthetic product to obtain a liquid phase of alcohol-water-oil and a tail gas mixture consisting of CO, H2, CO2, C1-C5 hydrocarbon, performing a low carbon alcohol synthesis reaction on a part of the tail gas mixture for recycling, and performing methanation on the other part of the tail gas mixture; separating oil from water in the liquid phase of the alcohol-water-oil to obtain an oil product and alcohol water, and separating alcohol from water in the alcohol-water mixture to obtain low carbon alcohol and water; performing methanation on the tail gas in the presence of the sulfur tolerant methanation catalyst and under the condition of methane conversion; condensing a methanation product to obtain a liquid phase of oil and alcohol water and a gas containing CH2, CO2, CO, H2, C2-C5 hydrocarbon, and performing the methanation on a part of the gas mixture of CH4, CO2, CO, H2, C2-C5 hydrocarbon for recycling; and sending the other part of the gas mixture to a CO2 separation device, and separating CO2 to obtain an SNG. The process has the advantages of having simple steps and low cost, organically coupling the low carbon alcohol synthesis process with the methanation process, improving the carbonutilization rate and realizing co-production and complementation of the low carbon alcohol and the natural gas.

Description

technical field [0001] The invention relates to a low-carbon alcohol synthesis process, in particular to a process for producing low-carbon alcohol and co-producing natural gas from synthesis gas under the action of a sulfur-resistant catalyst. Background technique [0002] Low carbon mixed alcohol refers to C 1 -C 6 The alcohol mixture has a wide range of uses. First of all, low-carbon alcohol itself is a good clean fuel. Secondly, low-carbon alcohols can be used as fuel additives such as gasoline due to their advantages such as high octane number, high calorific value, anti-explosion and shock resistance, good miscibility with gasoline, and reduced formaldehyde content in exhaust gas after combustion. Thirdly, low-carbon mixed alcohols can be separated to obtain products such as A, B, C, B, and amyl alcohol, which can be used as synthetic raw materials for other chemical products. The research on the direct synthesis of low-carbon mixed alcohols from syngas began in 19...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
IPC IPC(8): C07C29/153C07C31/02C10L3/08
Inventor 孙予罕张明伟李德宝姜东房克功林明桂
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products