Method for producing polysilicon
A production method, polysilicon technology, applied in the direction of chemical instruments and methods, silicon, silicon compounds, etc., can solve the problems of high equipment and operation requirements, achieve the effect of reducing unit production cost, high polysilicon deposition rate, and promoting mass transfer
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Embodiment 1
[0102] In this example, the reaction pressure in the reduction furnace was controlled at 0.3 MPa, and the reaction temperature was controlled at 1100°C.
[0103] At the beginning (0 moment) of the manufacturing method, hydrogen and trichlorosilane are respectively charged at 35.8Nm 3 / h and 5.5Nm 3 The intake air of / h is continuously fed into the reduction furnace. At this time, the molar ratio Q value was 6.5.
[0104] First, use the time of 45 hours to make the molar ratio Q with the above expression of the aforementioned first-order piecewise function (wherein the a value, b value, c value and d value of the first-order piecewise function expression are passed according to the aforementioned in the specification sheet) Calculation method to determine, omitted here, hereinafter the same) continuously decreased to 2.5, at the same time, within the aforementioned range, the intake flow rate of hydrogen and trichlorosilane increased linearly and continuously to 96.8Nm respec...
Embodiment 2
[0120] In this embodiment, the reaction pressure in the reduction furnace is controlled at 0.3 MPa, and the reaction temperature is controlled at 1080°C.
[0121] At the beginning (0 moment) of the manufacturing method, hydrogen and trichlorosilane are respectively charged at 42.7Nm 3 / h and 6.1Nm 3 The intake air of / h is continuously fed into the reduction furnace. At this time, the molar ratio Q is 7.
[0122] First, use the time of 45 hours to make the molar ratio Q with the above expression of the aforementioned first-order piecewise function (wherein the a value, b value, c value and d value of the first-order piecewise function expression are passed according to the aforementioned in the specification sheet) It is determined by calculation method, omitted here, the same below) continuously decreases to 3.0, at the same time, within the aforementioned range, the intake flow rate of hydrogen and trichlorosilane increases linearly and continuously to 118.5Nm with the inc...
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