US 5,958,138 AGranted

Gas recovery unit

AssigneeTeisan Kabushiki Kaisha

InventorsShinji Tomita, Shigeyoshi Nozawa

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Abstract

Provided is a gas recovery unit which is more efficient in its recovery and less expensive to run. The gas recovery unit comprises a CVD device, an exhaust gas recovery part and an exhaust gas purification part. The exhaust gas recovery part is constructed so as to have an inert gas reservoir part capable of accommodating liquid nitrogen, to have an exhaust gas supply part for supplying an exhaust gas to said inert gas reservoir part so that it can be brought in gasliquid contact with the liquid nitrogen, and to have a recovered and liquefied gas discharge part for discharging the recovered and liquefied gas which has been liquefied in the inert gas reservoir part. The exhaust gas purification part is constructed so as to have a recovered and liquefied gas reception part, an evaporator and a condenser for carrying out a heat exchange between said liquid nitrogen and the recovered and liquefied gas which has been evaporated, and cleaning gas recovery parts, and to have a cooling inert gas discharge part, wherein the cooling inert gas discharge part is connected to the inert gas supply path.

Claims10

Dependent claims

A gas recovery unit which comprises:

a CVD device with a gas introduction part having an inert gas supply path for supplying a diluting inert gas and a cleaning gas supply path for supplying a cleaning gas, each connected thereto, and which has an exhaust gas discharge part for releasing an exhaust gas;
and
an exhaust gas recovery part for cooling down and recovering said cleaning gas from said CVD device and an exhaust gas purification part for purifying the liquefied and recovered exhaust gas;
characterized in that:
said diluting inert gas is comprised of a gas having a boiling point lower than that of said cleaning gas,
in that said exhaust gas recovery part is constructed so as to have an inert gas reservoir part capable of accommodating a cooling inert gas having a boiling point lower than that of said cleaning gas in a liquid state, to have an exhaust gas supply part for supplying said exhaust gas to said inert gas reservoir part so that it can be brought in gas-liquid contact with said cooling inert gas, and to have a recovered and liquefied gas discharge part for discharging the recovered and liquefied gas which has been liquefied in said inert gas reservoir part,
in that said exhaust gas purification part is constructed so as to have a recovered and liquefied gas reception part provided for receiving the recovered and liquefied gas from said exhaust gas recovery part, to have an evaporator for evaporating said recovered and liquefied gas, a condenser for carrying out a heat exchange between the cooling inert gas in the liquid state consisting of the same composition as said diluting inert gas and said recovered and liquefied gas which has been evaporated, and cleaning gas recovery parts for recovering the cleaning gas which has been condensed in said condenser, and to have a cooling inert gas discharge part for discharging said cooling inert gas which has been evaporated;
and in that the cooling inert gas discharge part is connected to said inert gas supply path.

5 more elements

A gas recovery unit, wherein an etching device is provided having a gas introduction part comprising an inert gas supply path for supplying a diluting inert gas and an etching gas supply path for supplying an etching gas, each connected thereto, and which has an exhaust gas discharge part for releasing an exhaust gas;

and
an exhaust gas recovery part for cooling down and recovering said etching gas from the exhaust gas from said etching device and an exhaust gas purification part for purifying the liquefied and recovered exhaust gas;
and in which
said diluting inert gas is comprised of a gas having a boiling point lower than that of said etching gas;
said exhaust gas recovery part is constructed so as to have an inert gas reservoir part capable of accommodating a cooling inert gas having a boiling point lower than that of said etching gas in a liquid state, to have an exhaust gas supply part for supplying said exhaust gas to said inert gas reservoir part so that it can be brought in gas-liquid contact with said cooling inert gas, and to have a recovered and liquefied gas discharge part for discharging the recovered and liquefied gas which has been liquefied in said inert gas reservoir part;
said exhaust gas purification part is constructed so as to have a recovered and liquefied gas reception part for receiving the recovered and liquefied gas from said exhaust gas recovery part, to have an evaporator for evaporating said recovered and liquefied gas, a condenser for carrying out a heat exchange between the cooling inert gas consisting of the same composition as said diluting inert gas and said recovered and liquefied gas which has been evaporated, and etching gas recovery parts for recovering the etching gas which has been condensed in said condenser, and to have a cooling inert gas discharge part for discharging said cooling inert gas which has been evaporated;
and
the cooling inert gas discharge part is connected to said inert gas supply path.

5 more elements

Dependencies are inferred from the claim text.

Facts

Application: 08/743,188Filed 5 Nov 1996
Priority: JP 7-2871436 Nov 1995
Granted: 28 Sep 1999
Term ends: Not estimatedThe source records don’t support an estimate.

Classification11 codes

B01D 53/002
Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g.…: by…
B01D 8/00
Cold traps
C23C 16/44
Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical…
C23C 16/4412
Characterised by the method of coating: details relating to the exhausts, e.g. pumps, filters, scrubbers, particle traps