Participants
| Role | Name | HCID | Charge |
|---|
| Reactant | Ammonia | HCID 222 | — |
| Reactant | Chlorotrimethylsilane | HCID 6397 | — |
| Product | Hexamethyldisilazane | HCID 13838 | — |
Reaction Steps
In a summary of the process shown in FIG. 1, liquid trimethylchlorosilane (TMCS) and gaseous ammonia are fed to the first of a set of two or more reactors where they combine to form "crude" HMDS and an ammonium chloride by-product slurry. As set forth below, the first stage of the set of two or more reactors is a high shear vessel in which the TMCS and ammonia mixture is subjected to continuous high shear agitation in a recirculating reactor loop. Ammonium chloride produced as a by-product is in a "prilled" form in the resultant slurry. The slurry is then optionally fed to a second high shear reactor to insure that a complete reaction of all TMCS occurs. Then, the slurry is passed to a centrifuge where the ammonium chloride crystals are removed. In the centrifuge, HMDS is removed from the solid ammonium chloride particles in the centrifuge cake by displacement of the HMDS with a non-reactive wash. Suitable washes may be hydrocarbons or a buffered saturated ammonium chloride water solution. The HMDS liquid filtrate passes on to a mix tank where solid sodium amide is added.
Provenance & Evidence
| DOI | 10.6084/m9.figshare.5104873.v1 |
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| Patent number | US04644076 |
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| Source dataset | uspto-grants-1987_02 |
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| ORD ID | ord-e843266739ee4e51afc2b3f6831ffbe6 |
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| Source note | uspto-grants-1987_02 |
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