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The ‘South-to-North Water Transfer’ in the conversion section”

2019-12-17View Original

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The water resources in our country are unevenly distributed between the north and the south; the North China Plain suffers from severe water shortages, while the Yangtze River basin has relatively abundant water resources. We know that a large-scale project to transfer water from the south to the north has already been implemented. In the contact process sulfuric acid conversion section, the heat distribution during primary and secondary conversion is also uneven; there is always an excess of heat available to heat the primary gas (coming from the SO2 drying tower), and a economizer or boiler is often required at the inlet of the absorption tower to remove this excess heat. However, the heat available to heat the secondary gas (from the intermediate absorption tower) is often insufficient, especially for acid production plants operating at low concentrations or with low load, such as those that produce acid from zinc smelting flue gases. It is evident that in most zinc smelting flue gas acid production plants in China, the inlet temperature of the subsequent beds is low, which affects the secondary conversion rate and the overall conversion rate. Another reason for the insufficient heat to heat the secondary gas is that the demister in the intermediate absorption tower (Tower 1) contains acid, which causes leakage in the heat and cold exchange tubes downstream; once these tubes become blocked, the heat transfer area decreases.
Reply #22019-12-17
Using two rotations and two suction cycles for acid production is a mistake in itself: it involves high resistance, repeated heating, high energy consumption, and fails to meet environmental standards; The one-turn-one-suction + renewable desulfurization process features low resistance and low energy consumption, achieving ultra-low emissions in terms of environmental protection; it reduces the cost per ton of acid by 15 yuan.
Reply #32019-12-17
The two-turn two-suction secondary conversion and secondary absorption section can be regarded as a tail suction. At present, no tail suction system is satisfactory in terms of energy consumption and cost.
Reply #42019-12-17
An energy imbalance indicates that the heat exchange process design is unreasonable
Reply #52019-12-26
Whether it is absorption-desorption or adsorption-desorption, there are more or less some issues at present
Reply #62019-12-26
There are no issues at present; it has low emissions, low energy consumption, and can operate for a long period of time. Welcome to communicate and conduct inspections.
Reply #72019-12-30
There are “no” problems at all; you’re a salesperson, right?

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