Method and system for providing supplemental refrigeration to an air separation plant
US-2017131029-A1 · May 11, 2017 · US
US10260802B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10260802-B2 |
| Application number | US-201615382917-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 19, 2016 |
| Priority date | Jun 30, 2016 |
| Publication date | Apr 16, 2019 |
| Grant date | Apr 16, 2019 |
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An apparatus for the production of air gases with variable liquid production by the cryogenic separation of air can include a cold box having a heat exchanger, and a system of columns; a pressure monitoring device; and a controller. The cold box can be configured to receive a purified and compressed air stream under conditions effective for cryogenically separating the air stream to form an air gas product. The apparatus may also include means for transferring the air gas product from the cold box to an air gas pipeline. The pressure monitoring device is configured to monitor the pipeline pressure, and the controller is configured to adjust the product pressure of the air gas product coming out of the cold box based upon the pipeline pressure and to further adjust liquid production from the cold box based on the adjusted product pressure.
Opening claim text (preview).
We claim: 1. An apparatus for the production of air gases by the cryogenic separation of air, the apparatus comprising: a) a main air compressor configured to compress air to a pressure suitable for the cryogenic rectification of air to produce a compressed humid air stream, the compressed humid air stream having a first pressure P o ; b) a front end purification system configured to purify the compressed humid air stream of water and carbon dioxide to produce a dry air stream having reduced amounts of water and carbon dioxide as compared to the compressed humid air stream; c) a booster compressor in fluid communication with the front end purification system, wherein the booster compressor is configured to compress a first portion of the dry air stream to form a boosted air stream, the boosted air stream having a first boosted pressure P B1 ; d) a cold box comprising a main heat exchanger, a system of columns having a double column composed of a lower pressure column and a higher pressure column, a condenser disposed at a bottom portion of the lower pressure column, and a liquid oxygen pump, wherein the cold box is configured to receive the boosted air stream and a second portion of the dry air stream under conditions effective to separate air to form an air gas product, wherein the air gas product is selected from the group consisting of oxygen, nitrogen, and combinations thereof; e) means for monitoring the pressure of a pipeline, wherein the pipeline is in fluid communication with the cold box, such that the pipeline is configured to receive the air gas product from the cold box, the air gas product having a first product pressure P P1 ; f) a controller configured to adjust one or more pressure set points of the apparatus based on the monitored pipeline pressure, wherein the one or more pressure set points of the apparatus comprises a discharge pressure of the liquid oxygen pump, a discharge pressure of the booster compressor, and a discharge pressure of the main air compressor; and g) means for adjusting liquid production from the cold box. 2. The apparatus as claimed in claim 1 , wherein the means for adjusting liquid production from the cold box further comprises a second controller configured to monitor liquid product data. 3. The apparatus as claimed in claim 2 , wherein the liquid product data is selected from the group consisting of local liquid inventory of liquid nitrogen, local inventory of liquid oxygen, spot pricing data for liquid nitrogen, spot pricing data for liquid oxygen, and combinations thereof. 4. The apparatus as claimed in claim 2 , wherein the liquid product data comprises spot pricing data for liquid oxygen. 5. The apparatus as claimed in claim 1 , wherein the liquid production from the cold box is a liquid selected from the group consisting of liquid nitrogen, liquid oxygen, and combinations thereof. 6. The apparatus as claimed in claim 1 , wherein means for adjusting liquid production from the cold box comprises a process controller, in communication with a plurality of flow indicators, pressure indicators, and control valves. 7. The apparatus as claimed in claim 1 , wherein the air gas product is oxygen and the pipeline is an oxygen pipeline. 8. The apparatus as claimed in claim 7 , wherein the liquid oxygen pump pressurizes liquid oxygen from the lower pressure column to the first product pressure P P1 . 9. An apparatus for the production of air gases by the cryogenic separation of air, the apparatus comprising: a cold box configured to receive a purified and compressed air stream under conditions effective for cryogenically separating the air stream to form an air gas product using a system of columns, wherein the purified and compressed air stream is at a feed pressure P F when entering the cold box, wherein the air gas product is selected from the group consisting of oxygen, nitrogen, and combinations thereof, wherein the cold box is configured to produce the air gas product at a product pressure P PO ; a main air compressor disposed upstream the cold box; a booster air compressor downstream the main air compressor and upstream the cold box; means for transferring the air gas product from the cold box to an air gas pipeline; a pressure monitoring device configured to monitor the pipeline pressure P PL ; and a controller configured to adjust the product pressure P PO of the air gas product coming out of the cold box based upon the pipeline pressure P PL , wherein the controller is further configured to adjust one or more pressure set points of the apparatus based on the monitored pipeline pressure, wherein the one or more pressure set points of the apparatus is selected from the group consisting of a discharge pressure of the booster air compressor, a discharge pressure of the main air compressor, and combinations thereof, wherein the controller is further configured to receive liquid product data, wherein the liquid product data comprises spot pricing data for liquid oxygen, wherein the controller is also configured to adjust liquid production from the cold box based on the liquid product data. 10. The apparatus as claimed in claim 9 , wherein the air gas product is oxygen, wherein the cold box comprises a main heat exchanger, a system of columns having a double column composed of a lower pressure column and a higher pressure column, a condenser disposed at a bottom portion of the lower pressure column, and a liquid air gas pump selected from the group consisting of a liquid oxygen pump, a liquid nitrogen pump, and combinations thereof. 11. The apparatus as claimed in claim 10 , wherein the controller is configured to communicate with the liquid oxygen pump and adjust a discharge pressure of the liquid oxygen pump. 12. The apparatus as claimed in claim 9 , wherein the controller is in communication with the pressure monitoring device. 13. The apparatus as claimed in claim 9 , further comprising means for withdrawing liquid oxygen from the cold box. 14. The apparatus as claimed in claim 9 , further comprising means for withdrawing liquid nitrogen from the cold box.
Variable air feed, i.e. "load" or product demand during specified periods, e.g. during periods with high respectively low power costs (F25J3/0483 takes precedence) · CPC title
Control strategy, e.g. advanced process control or dynamic modeling · CPC title
the fluid being oxygen · CPC title
of main feed air · CPC title
Details about pipelines, i.e. network, for feed or product distribution · CPC title
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