Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Process method for preparing synthesis gas by using zero carbon or negative carbon emission system

A technology of an emission system and a process method, which is applied in the field of synthesis gas preparation, can solve the problems of complex process system control, low hydrogen and carbon content of synthesis gas, inability to directly use methanol for synthesis or Fischer-Tropsch process, etc., so as to simplify the control conditions of the process system and realize the Zero or negative carbon emissions, the effect of reducing greenhouse gas emissions

Active Publication Date: 2015-06-17
SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI +1
View PDF8 Cites 14 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, this process cannot realize the efficient utilization of carbon dioxide, therefore, the reduction of greenhouse gas emissions and the recycling of carbon resources of energy chemicals cannot be carried out
[0006] Chinese Patent No. 200710177471.X's "Methane Reforming Method and System for Coal Gasification Sensible Heat Polygeneration Energy Method and System" also mentioned the characteristics of carbon-rich gasification gas and hydrogen-rich reforming reaction gas, according to the characteristics of chemical products Production requires mixing the two in different proportions, eliminating the need for conversion processes in the production process of traditional coal-based chemical products. However, this process also cannot achieve efficient use of carbon dioxide
However, the process system control is complex
[0008] Therefore, in the existing synthesis gas preparation process, in order to achieve a suitable hydrogen-to-carbon ratio, a large amount of carbon dioxide is produced by the CO shift reaction or the resource utilization of carbon dioxide cannot be realized, or the synthesis gas produced by a single carbon dioxide-methane reforming reaction has a low hydrogen-to-carbon ratio and cannot Directly used in methanol synthesis or the defect of Fischer-Tropsch process, it is necessary to develop a synthesis gas preparation method that can not only improve carbon utilization efficiency but also realize resource utilization of greenhouse gases

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
  • Process method for preparing synthesis gas by using zero carbon or negative carbon emission system

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Refined desulfurized natural gas (sulfur content <1ppm) with a flow rate of 182.64kmol / hr, a pressure of 4.2MPa, and a temperature of 360°C is divided into two streams by a splitter, one with a flow rate of 100kmol / hr, demethane-steam reforming (first feed gas), another demethane-carbon dioxide reforming reactor (second feed gas).

[0037] After the first raw material gas is mixed with medium-pressure steam (steam) with a flow rate of 300kmol / hr, a pressure of 4MPa and a temperature of 370°C, it enters the convection section of the external heating type first-stage furnace after heat exchange, and the temperature rises to 600°C before entering the first-stage furnace A reforming reaction occurs, resulting in a first reformed gas. Among them, the operating pressure of the first stage furnace is 4MPa, the outlet temperature is 708°C, and the molar content of residual methane is 12.5%.

[0038] Pure oxygen from air separation, with a flow rate of 39 kmol / hr, undergoes com...

Embodiment 2

[0042] The flow rate is 157.09kmol / hr, the pressure is 3.8MPa, and the temperature is 358℃. The finely desulfurized coke oven gas (sulfur content <1ppm) has a hydrogen molar content of 58% and a methane molar content of 28.7%. Units, one with a flow rate of 100kmol / hr, demethane-steam reforming (first raw material gas), and another demethane-carbon dioxide reforming unit (second raw material gas).

[0043] Since the methane content in the first raw material gas is relatively low, after mixing with medium-pressure steam with a flow rate of 85 kmol / hr, a pressure of 4 MPa, and a temperature of 370 °C, the temperature rises to At 600°C, it enters the first-stage furnace for reforming reaction to obtain the first reformed gas. Among them, the operating pressure of the first stage furnace is 4MPa, and the outlet temperature is 750°C. The molar content of residual methane was 12.8%.

[0044] Pure oxygen from air separation, with a flow rate of 14.5kmol / hr, undergoes combustion rea...

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 present invention discloses a process method for preparing synthesis gas by using a zero carbon or negative carbon emission system. The process method comprises that: 1) first raw material gas is subjected to desulfurization, steam is matched, pressurization and heating are performed, a reaction is performed to obtain first conversion gas, the first conversion gas is output, the output first conversion gas and pure oxygen are mixed and then enter a two-stage furnace to react so as to obtain second conversion gas, and the second conversion gas is output from the two-stage furnace; 2) second raw material gas is subjected to desulfurization, pressurization and heating and then is mixed with pure oxygen and carbon dioxide, then a reforming reaction is performed to obtain third conversion gas, and the third conversion gas is output from the reforming reactor; and 3) the second conversion gas is subjected to heat recovery and then is mixed with the third conversion gas to form crude synthesis gas, wherein the crude synthesis gas is adopted as the subsequent synthesis gas with or without a decarbonization device. According to the present invention, the greenhouse gas emission is reduced, the carbon efficiency is improved, the recycling of the carbon resources of the energy source chemicals is achieved, the hydrogen-carbon ratio of the synthesis gas achieves the ideal ratio of the downstream process requirement, and the zero carbon or negative carbon emission of the whole system is achieved.

Description

technical field [0001] The invention relates to a process method for preparing synthesis gas, in particular to a process method for preparing synthesis gas using a zero-carbon or negative carbon emission system. Background technique [0002] In 2005, in response to the trend of continuous warming of the national climate, in order to protect human beings from the threat of drastic climate change, the Kyoto Protocol to reduce carbon dioxide emissions was promulgated. Therefore, the reduction and effective use of carbon dioxide emissions have become an urgent issue. Using carbon dioxide as a carbon and oxygen resource to prepare synthesis gas through high-temperature catalytic conversion has become an important way for large-scale chemical utilization of carbon dioxide. Using two greenhouse gases, methane and carbon dioxide, to carry out reforming reactions to prepare synthesis gas can not only achieve direct reduction of carbon dioxide emissions under low-carbon scenarios, but...

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
Patent Type & Authority Applications(China)
IPC IPC(8): C01B3/34
CPCY02P20/10Y02P30/00
Inventor 孙予罕唐志永赵铁均陈倩倩汪丹峰祝贺沈国飞黄巍王东飞章清
Owner SHANGHAI ADVANCED RES INST CHINESE ACADEMY OF SCI
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products