A kind of desulfurization gypsum calcination process with natural gas as heat source
A calcination process and desulfurized gypsum technology, which is applied in the field of desulfurized gypsum calcination process, can solve the problems of no research, desulfurized gypsum products affecting water consumption, and plastic cracking of buildings.
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Embodiment 1
[0026] The desulfurized gypsum calcination process using natural gas as a heat source provided in this embodiment is based on the calcination device disclosed in the patent CN211255729U. The calcination process does not specifically limit the circulation operation therein, and therefore does not involve the process control of the circulation link, only the main process path of drying-transportation-calcination is limited.
[0027] The desulfurized gypsum calcination process comprises the following steps:
[0028] S1, drying the wet gypsum material in a rotary dryer to obtain dry gypsum with a moisture content of less than 1%.
[0029] The average particle size of the wet gypsum material derived from the feeding system is 35 μm to 40 μm.
[0030] The gypsum wet material in this embodiment is controlled at a feed rate of 13 t / h, and during the drying process, the inlet temperature of the rotary dryer is controlled to be 600° C., and drying is performed for 10 minutes.
[0031]...
Embodiment 2
[0036] The desulfurized gypsum calcination process using natural gas as a heat source provided in this embodiment is based on the calcination device disclosed in the patent CN211261831U. The calcination process does not specifically limit the circulation operation therein, and therefore does not involve the process control of the circulation link, only the main process path of drying-transportation-calcination is limited.
[0037] The desulfurized gypsum calcination process comprises the following steps:
[0038] Q1. Dry the wet gypsum material in a rotary dryer to obtain dry gypsum with a moisture content of less than 1%.
[0039] The average particle size of the wet gypsum material derived from the feeding system is 35 μm to 40 μm.
[0040] The gypsum wet material in this embodiment is controlled at a feed rate of 16 t / h. During the drying process, the inlet temperature of the rotary dryer is controlled to be 750° C., and the drying is performed for 20 minutes.
[0041] Q2...
Embodiment 3
[0053] This example and Example 2 are carried out based on the same calcination device, and the same parts as in Example 2 will not be repeated, and only the parts different from those in Example 2 will be described. This embodiment differs from Embodiment 2 in that:
[0054] In step Q1, the average particle size of the wet gypsum material used in this embodiment is 30 μm˜33 μm.
[0055] In step Q3, the bucket elevator lifts the dry gypsum to a height of 15m, and then falls into the calciner after passing through the dispersing machine; and the lifting speed of the elevator is controlled to be 0.3m / s~0.5m / s.
[0056] In step Q4, the frequency conversion Roots fan is adjusted to 48Hz to ensure that the pressure in the calciner is kept at 25kPa, and the dry gypsum is calcined at 150°C for 25min in the calciner to obtain a standard consistency of 0.59 and a crystal water content of 5.7%. desulfurized gypsum powder.
[0057] The desulfurized gypsum powder obtained in this exampl...
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