US2014298669A1PendingUtilityA1

Apparatus and method for drying substrates

Assignee: SEMES CO LTDPriority: May 23, 2007Filed: May 2, 2014Published: Oct 9, 2014
Est. expiryMay 23, 2027(~0.8 yrs left)· nominal 20-yr term from priority
H10P 72/0414H10P 72/0408H10P 70/20F26B 21/40F26B 3/00F26B 21/14
52
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Claims

Abstract

A method for drying substrates using isopropyl alcohol (IPA) includes: a pre-stage in which heated fluid is injected to a bottom surface of a substrate to raise a temperature of the substrate simultaneously to injection of an organic solvent to a top surface of the substrate and injection of a dry gas to the top surface thereof to improve a vaporization power of the organic solvent; and a final stage in which the injection of the heated fluid is stopped and the organic solvent and the dry gas are injected to the top surface of the substrate.

Claims

exact text as granted — not AI-modified
1 . An apparatus for drying substrates, comprising:
 a support unit including a spin head rotating a substrate;   a bowl configured to accommodate the spin head of the support unit and provide a space where a process is performed;   an upper nozzle part configured to supply a dry fluid to a top surface of the substrate while the spin head rotates the substrate;   a lower nozzle part installed at a top surface of the spin head and configured to inject heated fluid to the bottom surface of the substrate simultaneously with the upper nozzle part supplying the dry fluid;   a first fluid supply part configured to supply the heated fluid to the lower nozzle part; and   a heater installed at the first fluid supply part and configured to heat fluid to be supplied to the lower nozzle part.   
     
     
         2 . The apparatus of  claim 1 , wherein the upper nozzle part includes:
 a first nozzle configured to inject an organic solvent to dry the top surface of the substrate; and   a second nozzle configured to inject a dry gas to improve vaporization power of the organic solvent.   
     
     
         3 . The apparatus of  claim 1 , further comprising a moving part configured to move the upper nozzle part such that the upper nozzle part injects fluid while moving from the center to the edge of a top surface of the substrate. 
     
     
         4 . The apparatus of  claim 1 , further comprising a lift configured to move up or down the bowl so that a height of the bowl is adjusted to a height of the spin head when the substrate is loaded on the spin head. 
     
     
         5 . The apparatus of  claim 4 , wherein the lift moves down the bowl so that the spin head protrudes over the bowl when the substrate is unloaded from the spin head. 
     
     
         6 . The apparatus of  claim 1 , wherein the lower nozzle part includes:
 a rinsing injection hole configured to inject a rinsing fluid; and   a drying injection hole configured to inject a drying fluid.   
     
     
         7 . The apparatus of  claim 6 , wherein the rinsing fluid is deionized water and the drying fluid is isopropyl alcohol or nitrogen gas. 
     
     
         8 . The apparatus of  claim 2 , wherein the organic solution is isopropyl alcohol and the dry gas is nitrogen gas. 
     
     
         9 . The apparatus of  claim 2 , wherein the first nozzle is closer to the center of the substrate than the second nozzle. 
     
     
         10 . The apparatus of  claim 2 , wherein the first and second nozzles are arranged in a moving direction of the upper nozzle part. 
     
     
         11 . The apparatus of  claim 2 , wherein the first and second nozzles are arranged tangentially to a moving direction of the upper nozzle part. 
     
     
         12 . The apparatus of  claim 1 , wherein the first fluid supply part includes:
 a supply line configured to provide the heated fluid from the heater to the lower nozzle part; and   a value configured to drain the heated fluid in the supply line for a predetermined time before the first fluid supply part supplies the heated fluid to the lower nozzle part.   
     
     
         13 . The apparatus of  claim 1 , wherein the heater heats the fluid at a temperature ranging from 60 to 80 degrees centigrade, and 
     
     
         14 . The apparatus of  claim 1 , wherein the bowl includes a plurality of recovery containers which recover different kinds of fluids, respectively.

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