Heat pump rectification dividing wall tower device for separating ultrapure trichlorosilane and operation method
An ultra-pure trichlorosilane, heat pump rectification technology, applied in the field of new energy-saving separation devices, heat pump rectification dividing wall tower equipment and devices, can solve the problems of reducing energy consumption in the separation process, low investment costs, small footprint, etc. Reach the effect of reducing equipment investment cost and reducing quantity
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Embodiment 1
[0018] Embodiment 1: Taking the raw material containing dichlorodihydrosilane, trichlorosilane and silicon tetrachloride as an example, the saturated liquid enters the partition tower with a flow rate of 10000kg / hr, and the system composition (dichlorodihydrosilane 10% , trichlorosilane 80% and silicon tetrachloride 10%). The number of theoretical plates in the main tower of the partition tower is 210, the number of theoretical plates in the pre-separation tower is 300, the feed position is the 85th theoretical plate of the pre-separation tower, the reflux ratio is 14.5, and the side line extraction position is in the 72nd block of the main tower Theoretical plate, the pressure at the top of the tower is 100kpa, the liquid distribution ratio at the top of the tower is 28.9%, and the gas distribution ratio at the bottom of the tower is 51.9%. The purity of the obtained trichlorosilane stream is 99.999943%, the yield reaches 91.25%, the energy consumption of the compressor is 50...
Embodiment 2
[0019] Embodiment 2: Taking the raw material containing dichlorodihydrosilane, trichlorosilane and silicon tetrachloride as an example, the saturated liquid enters the partition tower with a flow rate of 10000kg / hr, and the system composition (dichlorodihydrosilane 10% , trichlorosilane 80% and silicon tetrachloride 10%). The number of theoretical plates in the main tower of the partition tower is 160, the number of theoretical plates in the pre-separation tower is 200, the feed position is the 70th theoretical plate of the pre-separation tower, the reflux ratio is 14, and the side line extraction position is in the 68th block of the main tower Theoretical plate, the pressure at the top of the tower is 280kpa, the liquid distribution ratio at the top of the tower is 39.4%, and the gas distribution ratio at the bottom of the tower is 43.5%. The purity of the obtained trichlorosilane stream is 99.999171%, the yield reaches 90.62%, the energy consumption of the compressor is 331....
Embodiment 3
[0020]Embodiment 3: Taking the raw material containing dichlorodihydrosilane, trichlorosilane and silicon tetrachloride as an example, the saturated liquid enters the partition tower with a flow rate of 10000kg / hr, and the system composition (dichlorodihydrosilane 10% , trichlorosilane 80% and silicon tetrachloride 10%). The number of theoretical plates in the main tower of the partition tower is 150, the number of theoretical plates in the pre-separation tower is 180, the feed position is the 70th theoretical plate of the pre-separation tower, the reflux ratio is 12.5, and the side line extraction position is in the 70th theoretical plate of the main tower Theoretical plate, the pressure at the top of the tower is 300kpa, the liquid distribution ratio at the top of the tower is 35.4%, and the gas distribution ratio at the bottom of the tower is 41.4%. The purity of the obtained trichlorosilane stream is 99.999334%, the yield reaches 89.99%, the energy consumption of the compr...
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