참여 물질
| 역할 | 이름 | HCID | 투입량 |
|---|
| 반응물 | 1-Dodecanol | HCID 8193 | — |
| 반응물 | Phosphorus trichloride | HCID 24387 | — |
| 생성물 | 1-Chlorododecane | HCID 8192 | 97.5% |
반응 단계
Into a reactor system in accordance with FIG. 1 there were pumped jointly per hour 1.65 kg lauryl alcohol (purity: 97%) and 0.41 kg phosphorus trichloride. The cooling was performed in reaction zone 1 in such a way that the outlet temperature was about 110° C. The residence time in reaction zone 1 was 5 minutes. Following preheating to 150° C for 2.5 minutes, the reaction mixture reached reaction zone 2 in which the reaction temperature was maintained with superheated steam at 165° C. The residence time in reaction zone 2 was 26 minutes. By means of a pressure maintenance valve, the entire reactor system was under a pressure of 30 atm. The product obtained in this manner separated out immediately into two phases. One obtained per hour 1.8 kg of the organic phase corresponding to a yield of 97.5% of lauryl chloride with respect to lauryl alcohol. The purity amounted to 95 weight-percent of lauryl chloride. The product contained 0.14 weight-percent of dilauryl ether. Space-time yield: 1.4 kg/hour, liter.
출처 및 근거
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| 특허 번호 | US04100210 |
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| 출처 데이터셋 | uspto-grants-1978_07 |
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| ORD ID | ord-cb3cd4aed159408cb283528801ba7e05 |
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| 출처 메모 | uspto-grants-1978_07 |
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