A process and system for combined production of lime and sulfur by gypsum reduction and oxidation cycle calcination
An oxidation cycle and process system technology, applied in the preparation/purification of sulfur, calcium/strontium/barium oxides/hydroxides, sulfur compounds, etc., can solve the problems of reducing the quality of quicklime and unable to co-produce various sulfur products. , to reduce the decomposition temperature, alleviate the shortage of sulfur resources, and realize the effect of resource utilization
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Embodiment 1
[0045] like figure 1 As shown in the figure, this embodiment provides a system for the combined production of lime and sulfur by gypsum reduction and oxidation cycle calcination, including a gypsum storage bin 1 for storing gypsum, a preheating and drying system 2, a reduction calciner 3, and a first high-temperature separator connected in sequence. 4. Oxidation calciner 5, second high temperature separator 6, quicklime cooler 7 and quicklime storage bin 8, the gas phase outlet of the first high temperature separator 4 is connected to the gas phase inlet of the preheating and drying system 2, and one of the outlets of the second high temperature separator 6 Connect the inlet of the reduction calciner. Usually, the reaction of CaS with oxygen at high temperature also has parallel and competitive reactions. In this example, the excess air coefficient of the redox section is limited. In the device of the present disclosure, a part of CaS reacts with oxygen to form CaO and SO2 A...
Embodiment 2
[0049] This embodiment provides a process for the combined production of lime and sulfur by gypsum reduction-oxidation cyclic calcination.
[0050] It includes the following steps:
[0051] The gypsum is stored in the gypsum storage bin 1, and the feeding amount is precisely controlled by the feeder and sent to the gypsum preheating and drying system 2 for preheating and drying. The high temperature heat source comes from the calcining flue gas discharged from the reduction calciner 3; The temperature of the gypsum is 600-1050 ℃, first enter the reduction calciner 3, in the reduction calciner 3 control the reaction temperature 700-1200 ℃ and control the reducing gas air coefficient and excess air coefficient, specifically, by controlling the reducing gas and The mixing ratio of air and the gas flow are precisely controlled by electric valves. to obtain high temperature, low reduction potential , the reaction conditions allow most of the CaSO4 to react A small amount of Ca...
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