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Calcium carbide tail gas desulfurization type depth conversion process

A technology of tail gas and calcium carbide, which is applied in the chemical industry, climate sustainability, hydrogen/synthesis gas production, etc., can solve the problems of narrow deoxidizer activation temperature zone, deactivation of deoxidizer over temperature, and high deoxidation investment, so as to reduce steam Consumption, reduced equipment investment and operating costs, and easy operation and control

Active Publication Date: 2017-11-24
WUHUAN ENG
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  • Abstract
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  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There is also an anaerobic conversion process, which prevents high-concentration CO conversion from overheating by adopting a high water-gas ratio scheme, and the steam consumption of this process is high.
At the same time, in order to prevent deactivation of the conversion catalyst, the existing calcium carbide tail gas sulfur-tolerant and sulfur-reversible conversion processes need to carry out rough deoxidation before conversion, but for high-concentration CO deoxidizers, palladium and other precious metals are often used, and the deoxidation investment is high. At the same time The active temperature range of this type of deoxidizer is narrow, and it is easy to cause deactivation of the deoxidizer over temperature.

Method used

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  • Calcium carbide tail gas desulfurization type depth conversion process
  • Calcium carbide tail gas desulfurization type depth conversion process
  • Calcium carbide tail gas desulfurization type depth conversion process

Examples

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Embodiment Construction

[0018] figure 1 It is the flow chart of calcium carbide tail gas anaerobic deep conversion process.

[0019] This example takes the sulfur anaerobic deep conversion process for hydrogen production as an example to describe in detail: the calcium carbide tail gas (see Table 1 for the main components) after purification and pretreatment to remove trace impurities such as sulfur and arsenic is preheated by the tail gas preheater E01. After heating to 150-200°C, it is divided into three strands, accounting for 15-30%, 30-40% and 30-55% of the total gas volume respectively. After the converted product gas returned after pressurization is mixed, the dry basis concentration of CO in the mixed gas is adjusted to 30-40%, and steam is added through 1# steam mixer SP01 to adjust the water-gas ratio to 0.5-0.7, and then the mixed gas is passed through 1# Tail gas preheater E02 is further heated to 300-330°C, and sent to 1# shift furnace R01 for shift reaction;

[0020] After passing thr...

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PUM

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Abstract

The invention relates to a calcium carbide tail gas desulfurization type deep conversion process, which solves the problems of complex flow, high investment cost and high operation cost in the existing process. The technical solution includes the following steps: Divide the calcium carbide tail gas into three strands after preheating, the first strand of calcium carbide tail gas and part of the converted product gas are mixed and mixed into steam steam, preheated by the 1# tail gas preheater, and then sent to the 1# converter for conversion; The shift gas from the 1# shift furnace is mixed with the second calcium carbide tail gas, and then sent to the 2# shift furnace for shift after being mixed with steam. The shift gas from the 2# shift furnace is sent to the 1# tail gas preheater and into #The mixed gas in front of the conversion furnace is mixed with the third calcium carbide tail gas after heat exchange and cooling, and then mixed with steam through the 3# steam mixer, preheated by the 2# tail gas heat exchanger, enters the 3# conversion furnace, and exits the 3# conversion furnace After the shifted gas has been further transformed or not, the shifted product gas is obtained through heat energy recovery and condensate separation. The invention has simple process, low investment cost and low operation cost.

Description

technical field [0001] The invention relates to a calcium carbide tail gas conversion process, in particular to a calcium carbide tail gas anaerobic deep conversion process. Background technique [0002] During the production of calcium carbide, a large amount of CO-rich calcium carbide furnace tail gas is produced. "Calbium carbide industry access conditions" (revised in 2007) clearly stated that "calcium carbide furnace gas must be comprehensively utilized". Recycling and utilization of calcium carbide tail gas is of great significance for energy saving, energy saving and emission reduction, and environmental protection. The main components of calcium carbide tail gas are: 70-85% carbon monoxide, 2-10% carbon dioxide, 1-8% nitrogen, 2-10% hydrogen, 0.3-1.0% oxygen, and sulfur, phosphorus, arsenic, chlorine, Trace impurities such as cyanide, tar and soot. Calcium carbide tail gas is a high calorific value mixed gas, which has a wide range of uses. It can not only be used...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/16C01B3/14
CPCC01B3/14C01B3/16C01B2203/0294Y02P20/10
Inventor 赵保林严义刚李繁荣王志峰邹隐文毛俊楠
Owner WUHUAN ENG
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