Cryogenic system for producing low-purity oxygen

Claim 2

A process for producing low-purity oxygen by low-temperature rectification of air comprising: (a) compressing feed air to at least 85 psia, (b) dividing the compressed air into a first part and second part, (c) mixing said first part as oxidant for a combustion stream with fuel, (d) igniting said combustion stream in a combustion zone at ignition pressure of at least 80 psia to heat said combustion stream, (e) expanding the heated combustion stream in a power turbine to lower pressure with the production of external work, (f) recovering at least part of said external work as energy for said compressing of feed air, (g) cooling said second part of compressed air, (h) introducing the cooled air to a higher pressure rectification stage having its upper end in heat exchange relation with the lower end of a lower pressure rectification stage, (i) separating said cooled air into oxygen-enriched and nitrogen-rich liquids in said higher pressure rectification stage, (j) transferring at least part of said liquids from step (i) to said lower pressure rectification stage for separation into low purity oxygen and nitrogen-rich gases, (k) operating said lower-pressure rectification stage at pressure at least 20 psi lower than the step (d) ignition pressure, (l) discharging a low-purity oxygen product stream and at least one nitrogen-rich gas stream from said lower pressure rectification stage, (m) compressing at least part of the nitrogen-rich gas discharged in step (l) to pressure at least equal to the step (d) ignition pressure, and (n) flowing the compressed nitrogen-rich stream into the combustion stream, upstream of said power turbine.

Claim 3

The process of claim 1 wherein the feed air is compressed to pressure of from 100 to 250 psia, and wherein the lower pressure rectification stage is operated at pressure at least 30 psi lower than the step (d) ignition pressure.

Claim 4

The process of claim 1 wherein the flow rate of said first part of compressed air exceeds that of said second part, and substantially all of the work produced in step (e) is used for compressing the feed air and compressing the nitrogen-rich gas flowed to the combustion stream.

Claim 5

The process of claim 1 wherein at least part of said compressed nitrogen-rich stream is injected into the combustion stream after the step (d) ignition.

Claim 6

The process of claim 1 wherein said power turbine is operated substantially at its optimum inlet pressure.

Claim 7

The process of claim 1 wherein said higher pressure rectification stage is operated substantially at its optimum operating pressure.

Claim 8

The process of claim 1 wherein the second part of said feed air is further compressed prior to cooling.

Claim 9

The process of claim 7 wherein said power turbine is operated substantially at its optimum inlet pressure and said higher pressure rectification stage is operated substantially at its optimum operating pressure.

Claim 10

The process of claim 7 further comprising compressing an additional feed air stream to at least 85 psia, cooling said additional feed air stream, and feeding the cooled additional feed air stream to said higher pressure stage.

Claim 11

The process of claim 9 wherein the mass flow rate of the additional feed air stream is substantially equal to the total mass flow rate of the product streams.

Claim 12

The process of claim 1 further comprising compressing an additional feed air stream to at least 85 psia, cooling said additional feed air stream, and feeding the cooled additional feed air stream to said higher pressure stage.

Claim 13

The process of claim 11 wherein the mass flow rate of the additional feed air stream is substantially equal to the total mass flow rate of the product streams.

Claim 14

The process of claim 1 further comprising work expanding said second part of compressed feed air prior to introducing same to said higher pressure rectification stage.

Claim 15

The process of claim 1 wherein the first part of said compressed feed air is further compressed.

Claim 16

The process of claim 14 wherein said power turbine is operated substantially at its optimum inlet pressure.

Claim 17

Apparatus for producing low-purity oxygen by low temperature rectification comprising: (a) a compressor for compressing feed air to pressure of at least 85 psia, (b) a combustion system comprising a combustion chamber, conduit means for flowing a first part of compressed feed air from compressor (a) to said combustion chamber, means for introducing fuel to said combustion chamber, and conduit means for flowing combusted gas from said combustion chamber to, (c) a turbine for expanding the combusted gas to lower pressure so as to produce external work, (d) means for transferring external work of turbine (c) to compressor (a), (e) means for cooling a second part of compressed feed air, (f) a double rectification column comprising a higher-pressure stage for operation at at least about 85 psia, a lower-pressure stage, and a heat exchanger joining the upper end of the higher-pressure stage and the lower end of the lower-pressure stage, separate conduit means for transferring oxygen-enriched and nitrogen-rich liquids from the higher-pressure stage to the lower-pressure stage, (g) conduit means for flowing the cooled second part of the compressed feed air to the higher-pressure stage for rectification therein, (h) a compressor for compressing nitrogen-rich gas to pressure of at least 85 psia, (i) conduit means for flowing nitrogen-rich gas from the lower-pressure rectification stage to compressor (h), (j) conduit means for flowing compressed nitrogen-rich gas from compressor (h) to combustion system (b), and (k) conduit means for discharging low-purity oxygen from said power-pressure rectification stage.

Claim 18

Apparatus for producing low-purity oxygen by low temperature rectification comprising: (a) a compressor for compressing feed air to pressure of at least 85 psia, (b) a combustion system comprising a combustion chamber, conduit means for flowing a first part of compressed feed air from compressor (a) to said combustion chamber, means for introducing fuel to said combustion chamber, and conduit means for flowing combusted gas from said combustion chamber to, (c) a turbine for expanding the combusted gas to lower pressure so as to produce external work, (d) means for transferring external work of turbine (c) to compressor (a), (e) means for cooling a second part of compressed feed air, (f) a double rectification column comprising a higher-pressure stage for operation at at least about 85 psia, a lower-pressure stage, and a heat exchanger joining the upper end of the higher-pressure stage and the lower end of the lower-pressure stage, separate conduit means for transferring oxygen-enriched and nitrogen-rich liquids from the higher-pressure stage to the lower-pressure stage, (g) conduit means for flowing the cooled second part of the compressed feed air to the higher-pressure stage for rectification therein, (h) a compressor for compressing nitrogen-rich gas to pressure of at least 85 psia, (i) conduit means for flowing nitrogen-rich gas from the lower-pressure rectification stage to compressor (h), (j) conduit means for flowing compressed nitrogen-rich gas from compressor (h) to combustion system (b), and (k) conduit means for discharging low-purity oxygen from said power-pressure rectification stage.

Claim 19

The apparatus of claim 16 further comprising means for transferring external work of turbine (c) to compressor (h).

Claim 20

The apparatus of claim 16 wherein conduit means (j) flows at least part of the compressed nitrogen-rich gas into combustion system (b) downstream of said combustion chamber.

Claim 21

The apparatus of claim 16 further comprising a booster compressor for further compressing the second part of the feed air.

Claim 22

The apparatus of claim 19 further comprising an auxiliary compressor for compressing an additional feed air stream to pressure of at least 85 psia, and conduit means for feeding said auxiliary feed air stream to said booster compressor.

Claim 23

A process for producing low-purity oxygen by low-temperature rectification of air comprising: (a) compressing feed air to at least 85 psia, (b) dividing the compressed air into a first part and second part, (c) mixing said first part as oxidant for a combustion stream with fuel, (d) igniting said combustion stream in a combustion zone at ignition pressure of at least 80 psia to heat said combustion stream, (e) expanding the heated combustion stream in a power turbine to lower pressure with the production of external work, (f) recovering at least part of said external work as energy for said compressing of feed air, (g) cooling said second part of compressed air, (h) introducing the cooled air to a higher pressure rectification stage having its upper end in heat exchange relation with the lower end of a lower pressure rectification stage, (i) separating said cooled air into oxygen-enriched and nitrogen-rich liquid in said higher pressure rectification stage, (j) transferring at least part of said liquids from step (i) to said lower pressure rectification stage for separation into low purity oxygen and nitrogen-rich gases, (k) operating said lower-pressure rectification stage at pressure at least 20 psi lower than the step (d) ignition pressure, (l) discharging a low-purity oxygen product stream and at least one nitrogen-rich gas stream from said lower pressure rectification stage, (m) compressing at least part of the nitrogen-rich gas discharged in step (l) to pressure at least equal to the step (d) ignition pressure, and (n) injecting said compressed nitrogen-rich stream into the combustion stream prior to the step (d) ignition.

Claim 24

A process for producing low-purity oxygen by low-temperature rectification of air comprising: (a) compressing feed air to at least 85 psia, (b) dividing the compressed air into a first part and second part, (c) mixing said first part as oxidant for a combustion stream with fuel, (d) igniting said combustion stream in a combustion zone at ignition pressure of at least 80 psia to heat said combustion stream, (e) expanding the heated combustion stream in a power turbine to lower pressure with the production of external work, (f) recovering at least part of said external work as energy for said compressing of feed air, (g) cooling said second part of compressed air, (h) introducing the cooled air to a higher pressure rectification stage having its upper end in heat exchange relation with the lower end of a lower pressure rectification stage, (i) separating said cooled air into oxygen-enriched and nitrogen-rich liquid in said higher pressure rectification stage, (j) transferring at least part of said liquids from step (i) to said lower pressure rectification stage for separation into low purity oxygen and nitrogen-rich gases, (k) operating said lower-pressure rectification stage at pressure at least 20 psi lower than the step (d) ignition pressure, (l) discharging a low-purity oxygen product stream and at least one nitrogen-rich gas stream from said lower pressure rectification stage, (m) compressing at least part of the nitrogen-rich gas discharged in step (l) to pressure at least equal to the step (d) ignition pressure, and (n) injecting said compressed nitrogen-rich stream into the combustion stream prior to the step (d) ignition.

Claim 25

Apparatus for producing low-purity oxygen by low pressure rectification comprising: (a) a compressor for compressing feed air to pressure of at least 85 psia, (b) a combustion system comprising a combustion chamber, conduit means for flowing a first part of compressed feed air from compressor (a) to said combustion chamber, means for introducing fuel to said combustion chamber, and conduit means for flowing combusted gas from said combustion chamber to, (c) a turbine for expanding the combusted gas to lower pressure so as to produce external work, (d) means for transferring external work of turbine (c) to compressor (a), (e) means for cooling a second part of compressed feed air, (f) a double rectification column comprising a higher-pressure stage for operation at at least about 85 psia, a lower-pressure stage, and a heat exchanger joining the upper end of the higher-pressure stage and the lower end of the lower-pressure stage, separate conduit means for transferring oxygen-enriched and nitrogen-rich liquids from the higher-pressure stage to the lower-pressure stage, (g) conduit means for flowing the cooled second part of the compressed feed air to the higher-pressure stage for rectification therein, (h) a compressor for compressing nitrogen-rich gas to pressure of at least 85 psia, (i) conduit means for flowing nitrogen-rich gas from the lower-pressure rectification stage to compressor (h), (j) conduit means for flowing at least part of the compressed nitrogen-rich gas into combustion system (b) upstream of said combustion chamber, and (k) conduit means for discharging low-purity oxygen from said lower-pressure rectification stage.

Claim 26

Apparatus for producing low-purity oxygen by low pressure rectification comprising: (a) a compressor for compressing feed air to pressure of at least 85 psia, (b) a combustion system comprising a combustion chamber, conduit means for flowing a first part of compressed feed air from compressor (a) to said combustion chamber, means for introducing fuel to said combustion chamber, and conduit means for flowing combusted gas from said combustion chamber to, (c) a turbine for expanding the combusted gas to lower pressure so as to produce external work, (d) means for transferring external work of turbine (c) to compressor (a), (e) means for cooling a second part of compressed feed air, (f) a double rectification column comprising a higher-pressure stage for operation at at least about 85 psia, a lower-pressure stage, and a heat exchanger joining the upper end of the higher-pressure stage and the lower end of the lower-pressure stage, separate conduit means for transferring oxygen-enriched and nitrogen-rich liquids from the higher-pressure stage to the lower-pressure stage, (g) conduit means for flowing the cooled second part of the compressed feed air to the higher-pressure stage for rectification therein, (h) a compressor for compressing nitrogen-rich gas to pressure of at least 85 psia, (i) conduit means for flowing nitrogen-rich gas from the lower-pressure rectification stage to compressor (h), (j) conduit means for flowing at least part of the compressed nitrogen-rich gas into combustion system (b) upstream of said combustion chamber, and (k) conduit means for discharging low-purity oxygen from said lower-pressure rectification stage.