초록 ▼

A vaporizer (film evaporator) (13) for halide-free, silicon-containing liquid reactants used in producing preforms is provided. The vaporizer includes a plurality of packed-bed columns (22) surrounding a central tube (24). A mixture of liquid reactant, e.g., octamethylcyclotetrasiloxane, and gas, e.

A vaporizer (film evaporator) (13) for halide-free, silicon-containing liquid reactants used in producing preforms is provided. The vaporizer includes a plurality of packed-bed columns (22) surrounding a central tube (24). A mixture of liquid reactant, e.g., octamethylcyclotetrasiloxane, and gas, e.g., oxygen, is sprayed onto the top surfaces (54) of the columns (22) by a set of spray nozzles (32). The liquid reactant and the gas flow downward together through the columns and are heated by hot oil (28) which flows around the columns' walls (50). The liquid reactant evaporates into the gas until the dew point temperature is reached, at which point all of the liquid reactant will have been converted into vapor. The vapor/gas mixture exits the bottom surfaces 56 of columns (22), where its direction of flow changes from downward to upward. This change in flow direction separates higher molecular weight species (46) from the vapor/gas mixture. The vapor/gas mixture leaves the vaporizer (13) through central tube (24) and is supplied to soot-producing burners (20) where it is used to produce preforms.

대표청구항 ▼

[ What is claimed is:] [1.] A method of providing reactant vapors to make a silicon dioxide containing preform by decomposing said reactant vapors to form particles, comprising:(a) providing a reactant in liquid form, at a first predetermined flow rate, said reactant being polymerizable to form a sp

[ What is claimed is:] [1.] A method of providing reactant vapors to make a silicon dioxide containing preform by decomposing said reactant vapors to form particles, comprising:(a) providing a reactant in liquid form, at a first predetermined flow rate, said reactant being polymerizable to form a species having a molecular weight higher than a molecular weight of the reactant;(b) providing a gas at a second predetermined flow rate;(c) providing a vertically-oriented, packed-bed column having a top surface and a bottom surface;(d) passing the liquid reactant and the gas through the packed-bed column with the liquid reactant and the gas both flowing downward within the column and with a maximum internal operating pressure within the column during such downward flow being P.sub.max ;(e) heating the packed-bed column to a temperature so that, before reaching the bottom surface of the column, the liquid reactant and the gas, at their predetermined flow rates, are heated to a temperature above a dew point temperature of the liquid reactant at P.sub.max, whereby the liquid reactant is vaporized before reaching the bottom surface and exits from the bottom surface as a mixture of the vaporized reactant and the gas (the vapor/gas mixture)is inserted;(f) separating the higher molecular weight species of the reactant from the vapor/gas mixture; and(g) delivering the vapor/gas mixture to a vapor utilization site to form said preform.