Apparatus for the production of air gases by the cryogenic separation of air with variable liquid production and power usage

Patent metadata

Field	Value
Publication number	US-10281206-B2
Application number	US-201715637035-A
Country	US
Kind code	B2
Filing date	Jun 29, 2017
Priority date	Jun 30, 2016
Publication date	May 7, 2019
Grant date	May 7, 2019

Abstract

An apparatus for the production of air gases 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 determine whether to operate in a power savings mode or a variable liquid production mode. By operating the apparatus in a dynamic fashion, a power savings and/or additional high value cryogenic liquids can be realized in instances in which the pipeline pressure deviates from its highest value.

First claim

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 comprised 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 ; and
f) a process 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 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 process controller is further configured to adjust liquid production from the cold box; and
wherein the process controller is further configured to choose between a first mode of operation and a second mode of operation, wherein the first mode of operation results in a power savings, wherein the second mode of operation results in increased liquid production.

2. The apparatus as claimed in claim 1 , wherein the process controller is further configured to access process conditions selected from the group consisting of spot pricing data for electricity, local liquid inventories, and combinations thereof.

3. The apparatus as claimed in claim 1 , wherein during the second mode of operation, the process controller is configured maintain the first boosted pressure P B1 substantially constant while adjusting the discharge pressure of the liquid oxygen pump.

4. The apparatus as claimed in claim 1 , wherein during periods of time in which the process controller chooses the second mode of operation, the first boosted pressure P B1 is kept substantially constant.

5. 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 , wherein the cold box is in fluid communication with an air gas pipeline, such that the apparatus, during operation, is configured to send an air gas product from the cold box to the air gas pipeline, wherein the system of columns comprises a double column comprised of a lower pressure column and a higher pressure column, wherein the cold box further comprises a main heat exchanger, a condenser disposed at a bottom portion of the lower pressure column, and a liquid oxygen pump configured to receive liquid oxygen from the system of columns and introduce the liquid oxygen to a cold end of the main heat exchanger;
a main air compressor disposed upstream the cold box;
a booster air compressor downstream the main air compressor and upstream the cold box;
a pressure monitoring device configured to monitor the pipeline pressure P PL ; and
a controller configured to operate the apparatus in a first mode of operation and a second mode of operation, 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, a discharge pressure of the liquid oxygen pump, 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 during the first mode of operation, the controller is further configured to reduce the difference between the pipeline pressure P PL and the discharge pressure of the liquid oxygen pump,
wherein during the second mode of operation, the controller is further configured to reduce the difference between the pipeline pressure P PL and the delivery pressure P DO ; and adjust liquid production from the cold box.

6. The apparatus as claimed in claim 5 , wherein the controller reduces the difference between the pipeline pressure P PL and the discharge pressure of the liquid oxygen pump by adjusting the discharge pressure of the liquid oxygen pump.

7. The apparatus as claimed in claim 5 , wherein the controller, during the second mode of operation, is configured to adjust the liquid production from the cold box while maintaining the feed pressure P F substantially constant.

8. The apparatus as claimed in claim 5 , wherein the product pressure P PO and the discharge pressure of the liquid oxygen pump are substantially the same.

9. The apparatus as claimed in claim 5 , wherein the controller is in communication with the pressure monitoring device.

10. The apparatus as claimed in claim 5 , comprising an absence of a GOX feed valve configured to reduce the difference between the pipeline pressure P PL and the delivery pressure P DO .

11. The apparatus as claimed in claim 5 , further comprising a gaseous oxygen (GOX) feed valve, wherein the GOX feed valve is in fluid communication with an outlet of the liquid oxygen pump and an inlet of the air gas pipeline, wherein the GOX feed valve is maintained in a fully open position during operation in both the first mode and second mode.

12. The apparatus as claimed in claim 5 , wherein during the first mode of operation, the controller is further configured to adjust the discharge pressure of the main air compressor.

13. The apparatus as claimed in claim 5 , wherein during the first mode of operation, the controller is further configured to adjust the discharge pressure of the booster compressor.

Assignees

• Air Liquide

Inventors

• Kong Paul
• Pham-Huy Minh
• Yip Wendy

Classifications

• F25J3/0257 Primary

  separation of nitrogen (from air F25J3/04, production of nitrogen in general C01B21/00) · CPC title

• F15B11/0423

  by controlling pump output or bypass, other than to maintain constant speed · CPC title

• B01D3/146

  Multiple effect distillation · CPC title

• F25J3/04412

  in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column · CPC title

• F25J2290/60

  Details about pipelines, i.e. network, for feed or product distribution · CPC title