초록 ▼

A method is disclosed for the purification of an organic heat transfer fluid without thermal degradation which comprises passing contaminated transfer fluid to a purification zone wherein the fluid is heated to produce a vapor-liquid phase in which the liquid fraction thereof is caused to flow in a

A method is disclosed for the purification of an organic heat transfer fluid without thermal degradation which comprises passing contaminated transfer fluid to a purification zone wherein the fluid is heated to produce a vapor-liquid phase in which the liquid fraction thereof is caused to flow in a narrow flowpath within the purification zone to insure maximum purification temperature and minimum purification zone vessel wall temperature. The heating may be effected by an electric resistance heating means such as bayonet-type electric heaters.

대표청구항 ▼

A method for the purification of a heat transfer fluid which is subject to thermal degradation and is used in a closed-end process system comprising a vaporizer containing an inventory of said heat transfer fluid and a heat sink, said method comprising: (a) withdrawing at least a portion of said hea

A method for the purification of a heat transfer fluid which is subject to thermal degradation and is used in a closed-end process system comprising a vaporizer containing an inventory of said heat transfer fluid and a heat sink, said method comprising: (a) withdrawing at least a portion of said heat transfer fluid inventory from said vaporizer in the liquid phase; (b) passing said withdrawn portion to a purification zone possessing electric resistance heating means; (c) heating said liquid portion within said purification zone by means of said heating means to form a vapor phase relatively lean in thermal degradation precursors and a liquid phase relatively rich in thermal degradation precursors possessing a temperature greater than about 600°F. at a pressure of 30 to 160 psig; (d) passing said relatively rich-liquid phase in a continuous flow pattern traversing a narrower flow path of 0.1 to 0.5 inches to effect a wall temperature of said purification zone of less than about 650°F. and to effect deposit of said thermal degradation precursors via gravity to the bottom portion of said purification zone; (e) withdrawing said vapor phase from said purification zone; (f) condensing said withdrawn vapor phase in a condenser zone to form a purified liquid heat transfer fluid; (g) passing said purified liquid heat transfer fluid to said vaporizer inventory; and (h) withdrawing at least intermittently said bottom portion of said purification zone to remove said thermal degradation precursors.