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A Syngas Shift Process

A synthesis gas and process technology, applied in hydrogen/synthesis gas production, inorganic chemistry, chemical instruments and methods, etc., can solve problems such as reducing reaction speed, and achieve the effect of low operating cost, simple and feasible operation

Active Publication Date: 2021-06-29
浙江天禄环境科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0017] Under industrial conditions, when catalyst particles with an equivalent diameter of 2-10 mm or larger are used, the internal diffusion of the shift reaction is severe, which reduces the reaction rate to a certain extent

Method used

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  • A Syngas Shift Process
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Examples

Experimental program
Comparison scheme
Effect test

preparation example

[0041]A synthesis gas shift process, the synthesis gas containing CO is passed through a pressurization device, pressurized to 1.5MPa-3.0MPa, passed into the shift device, and water vapor is passed at the same time, in the presence of a shift catalyst, and the shift The temperature of the device is 150-1000°C, CO and water react to obtain a shift gas in which H 2 The molar ratio to CO is not less than 2.9.

[0042] The raw material low-rank coal of the present invention can be pulverized coal or lump coal, and when the low-rank coal adopts lump coal, the oversized lump coal can be processed by crushing and screening to obtain pulverized coal with smaller particle size. It is preferred to use pulverized coal as a raw material. On the one hand, pulverized coal does not need to be crushed and screened, which saves process steps. The heating area during drying is large and the drying efficiency is high. On the other hand, pulverized coal is relatively cheap compared to lump coal. ...

experiment example 1

[0049] A synthesis gas shift process, the synthesis gas containing CO is passed through a pressurization device, pressurized to 1.5MPa-3.0MPa, passed into the shift device, and water vapor is passed at the same time, in the presence of a shift catalyst, and the shift The temperature of the device is 150-1000°C, CO and water react to obtain a shift gas in which H 2 The molar ratio to CO is not less than 2.9.

[0050] In Experimental Example 1, the synthesis gas sent from the previous section was pressurized at 1.5-3.0MPa, and the temperature was raised by 150-500°C through the heat exchanger, and then mixed with the self-produced steam from the synthesis to control the appropriate water-gas ratio Entering the shift furnace, the temperature of the shift gas exiting the shift furnace is 300-500°C, and the temperature of the shift gas is exchanged with the raw material gas through a heat exchanger to lower the temperature, and then the temperature is lowered by 10-50°C through the...

experiment example 2

[0054] Experimental Example 2 refers to Experimental Example 1. The difference is that in the shift process of Experimental Example 2, before the synthesis gas is passed into the shifter, it flows through the first preheating device and is preheated to 150-250°C. Before the steam is passed into the conversion device, it flows through the second preheating device and is preheated to 200-1000°C. The purpose is to more accurately control the reaction temperature of the transformation reaction.

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Abstract

The invention discloses a synthesis gas conversion process. The synthesis gas containing CO is pressurized to 1.5MPa-3.0MPa through a pressurization device, and then passed into the conversion device, and water vapor is simultaneously passed into the conversion catalyst in the presence of a conversion catalyst. The temperature of the shift device is 150‑1000°C, CO and water react to obtain shift gas, in which H 2 The molar ratio to CO is not less than 2.9. Under anaerobic or microaerobic conditions, the dried low-rank coal is prepared to mainly contain CO and H 2 The synthesis gas, through the conversion process of the present invention, adjust the CO and H of the synthesis gas 2 ratio, so that the synthesis gas can be used to synthesize methane, and then make full use of low-rank coal; the conversion process of the present invention is simple and feasible to operate, uses existing equipment, and has low operating costs, which is suitable for industrial production.

Description

technical field [0001] The invention relates to the technical field of clean utilization of coal substances, in particular to a synthesis gas conversion process. Background technique [0002] More than half of my country's proven coal reserves are low-rank coals, and the volatile matter contained in them is equivalent to 100 billion tons of oil and gas resources. Low-rank coal mainly has the material characteristics of high moisture and high volatility. When burning, the flame is long and smokey, and the degree of coalification is low. Typical coal types are lignite and long-flame coal. my country is rich in coal and lacks oil and gas. How to efficiently utilize low-rank coal has become a major issue in today's clean coal technology. However, whether it is combustion power generation or modern coal chemical utilization, the efficiency of comprehensive utilization is extremely low because of its three characteristics of high water, high ash and low calorific value. [0003]...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/16
CPCC01B3/16C01B2203/0283
Inventor 冯政涵何巍李勇熊德芳黄成侃杨兰花吕彬峰
Owner 浙江天禄环境科技有限公司