A kind of method utilizing the tail gas of 3-chloropropyl trichlorosilane to prepare polysiloxane
A technology of chloropropyltrichlorosilane and polysiloxane, which is applied in the field of preparing polysiloxane from the production tail gas of 3-chloropropyl trichlorosilane, which can solve the problem of increased difficulty, difficult handling, and increased cost of tail gas treatment equipment Check the shutdown time and other issues to achieve the effect of increasing lipophilicity, reducing production costs and environmental protection pressure
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Embodiment 1
[0037] The exhaust gas discharged from the 3-chloropropylene trichlorosilane synthesis apparatus is frozen and pressurized to 0.05 MPa, and then the ethanol absorbing liquid receiving device is supplied with -35 ° C freezing water in the ethanol absorbing liquid receiving device. Insulation, passed through ethanol absorption liquid into the water absorption system; after continuous exhaust gas 48h, the esterification reaction was obtained, and the gas phase analysis was taken, and the ethanol content of the esterification reaction was 26%, water. The hydrochloric acid made of absorbing system is transparent, no suspension liquid; transfer the esterification reaction to the synthesis device, the synthesis device is negative pressure -0.085MPa, and heat insulation at 35 ° C to 45 ° C for 2 h to no gas spill; The device is tapered to 50 ° C, and the molar ratio of 2: 1 is added dropwise at 50 ° C to 55 ° C, and the mixed solution is 0 (gas chromatographic detection), and then the fir...
Embodiment 2
[0039] The exhaust gas discharged from the 3-chloropropylene trichlorosilane synthesis apparatus is frozen and pressurized to 0.2 MPa, and then the ethanol absorbing liquid receiving device is supplied with -15 ° C. Insulation, passed through ethanol absorption liquid into the water absorbing system; after continuous exhaust 48h, the esterification reaction was obtained, and the gas phase analysis was sampled, and the ethanol content of the esterification reaction was 22%, water. The hydrochloric acid made of absorbing system is transparent, no suspension liquid; transfer the esterification reaction to the synthesis device, the synthesis device is negative pressure -0.085MPa, and heat insulation at 35 ° C to 45 ° C for 2 h to no gas spill; The device is tapered to 50 ° C, and the molar ratio of 2: 1 is added dropwise at 50 ° C to 55 ° C, and the mixed solution is 0 (gas chromatographic detection), and then the first pressure distillation is then reduced. Ethanol is evaporated, and...
Embodiment 3
[0041]The exhaust gas discharged from the 3-chloropropylene trichlorosilane synthesis apparatus is frozen and pressurized to 0.15 MPa, and then the ethanol absorbing liquid receiving device is supplied with -15 ° C. Insulation, passed through ethanol absorption liquid into the water absorption system; after continuous exhaust gas 48h, the esterification reaction was obtained, and the gas phase analysis was sampled, and the ethanol content of the esterification reaction was 23%, water. The hydrochloric acid made of absorbing system is transparent, no suspension liquid; transfer the esterification reaction to the synthesis device, the synthesis device is negative pressure -0.085MPa, and heat insulation at 35 ° C to 45 ° C for 2 h to no gas spill; The device is tapered to 50 ° C, and the molar ratio of 2: 1 is added dropwise at 50 ° C to 55 ° C, and the mixed solution is 0 (gas chromatographic detection), and then the first pressure distillation is then reduced. Ethanol was evaporate...
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