Processing unit for boiler cleaning connector of supercritical unit and cleaning process thereof
A technology for cleaning supercritical units and boilers, which is applied in the field of pickling and can solve the problems of rising tube wall temperature, easy falling off and accumulation, and hidden safety hazards.
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Embodiment 1
[0038] The cleaning process of the present invention is as follows: first, the ammonia washing medium mainly composed of 2% ammonia water, 0.5% ammonium persulfate, 0.3% corrosion inhibitor and the rest of water is used for 4 hours at a temperature of 30°C. Then flush with desalinated water, and after flushing, use a compound organic acid mainly composed of 6% glycolic acid compounded formic acid with a mass ratio of 1:0.2, 0.2% corrosion inhibitor monoethanolamine, and 0.5% thiourea and hydrogen fluoride The pickling medium composed of ammonium additives and the balance of water at a mass ratio of 1.5:1 is used for the first pickling at a temperature of 50°C. The pickling time is controlled at 10 hours and the pH is 4.5. After pickling, rinse with desalinated water again, and then use 5% catalytic citric acid, 0.3% corrosion inhibitor, 0.5% thiourea and ammonium bifluoride in a mass ratio of 1.8:1 to form an auxiliary agent and residual A pickling medium composed of a certain...
Embodiment 2
[0040] The cleaning process of the present invention is as follows: firstly, the ammonia washing medium mainly composed of 2.5% ammonia water, 0.7% ammonium persulfate, 0.35% corrosion inhibitor and the rest of water is used for ammonia washing at 40° C. for 3 hours. Then flush with desalinated water, and after flushing, use mainly 5% of catalytic citric acid, 0.3% of corrosion inhibitor monoethanolamine, 0.8% of auxiliary agents composed of thiourea and ammonium bifluoride in a mass ratio of 1.6:1 and the balance The pickling medium composed of water was first pickled at a temperature of 75°C, the pickling time was controlled at 8 hours, and the pH was 5. After pickling, rinse with desalinated water again, and then use 4% ethylenediaminetetraacetic acid, 0.3% corrosion inhibitor, 0.8% thiourea and ammonium bifluoride in a mass ratio of 1.8:1. The acid pickling medium composed of agent and the rest of water is subjected to the second pickling at a temperature of 80°C, the pick...
Embodiment 3
[0042] The cleaning process of the present invention is as follows: first, the ammonia washing medium mainly composed of 3% ammonia water, 0.8% ammonium persulfate, 0.4% corrosion inhibitor and the rest of water is used for 2 hours at a temperature of 50°C. Then flush with desalinated water, and after flushing, use 5% ethylenediaminetetraacetic acid, 0.4% corrosion inhibitor monoethanolamine, 1% additives composed of thiourea and ammonium bifluoride in a mass ratio of 2:1 and The pickling medium composed of the remaining water was first pickled at a temperature of 90°C, the pickling time was controlled at 6 hours, and the pH was 5.5. After pickling, rinse with desalinated water again, and then use 4% compound organic acid composed of glycolic acid compound fluoride with a mass ratio of 1:0.5, 0.4% corrosion inhibitor, 1% thiourea The pickling medium composed of ammonium bifluoride and ammonium bifluoride in a mass ratio of 1.8:1 to form an auxiliary agent and the rest of water...
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