Method for operating an industrial plant with an adsorption device and industrial plant with an adsorption device

Patent metadata

Field	Value
Publication number	US-11149907-B2
Application number	US-201716312007-A
Country	US
Kind code	B2
Filing date	Jun 21, 2017
Priority date	Jun 23, 2016
Publication date	Oct 19, 2021
Grant date	Oct 19, 2021

Abstract

In a method for operating an adsorption device a laden gas stream is fed to an inlet of a sorption buffer device. In the device the laden gas stream passes through a sorbent for receiving a loading of sorbable substance along a sorption path from the inlet to an outlet. The sorbable substance passes from the gas stream to the sorbent, or vice versa, depending on the loading of the gas stream and the sorbent. During a phase of elevated loading, a region with an elevated loading of the sorbent extends from the inlet along the sorption path. During a phase of reduced loading, the region with the elevated loading of the sorbent is shifted in the direction toward the outlet. Length of the sorption path and quantity of the sorbent in the sorption buffer device are selected for accommodating at least three different regions of elevated loading.

First claim

The invention claimed is:

1. A method for operating an industrial plant ( 100 ) having an adsorption device ( 10 ) which emits a gas stream (G 1 ) laden with a sorbable substance with a predefined mass flow rate,
wherein phases (P 1 ) of reduced loading (φ 1 ) and phases (P 2 ) of elevated loading (φ 2 ), which follow one another in a temporally alternating manner, are involved for the laden gas stream (G 1 ), said method comprising:
feeding ( 710 ) the laden gas stream (G 1 ) to an inlet ( 42 ) of a sorption buffer device ( 40 );
conducting ( 720 ) the laden gas stream (G 1 ) in the sorption buffer device ( 40 ) through a sorbent ( 44 ), which is suitable for receiving a loading (ψ) of the sorbable substance, along a sorption path ( 45 ), which leads from the inlet ( 42 ) to an outlet ( 43 ) of the sorption buffer device ( 40 ), wherein the sorbable substance passes from the gas stream to the sorbent ( 44 ), or from the sorbent ( 44 ) to the gas stream, in dependence on the loading of the gas stream (φ) and the loading of the sorbent (ψ); and
withdrawing ( 730 ) a treated gas stream (G 4 ) at the outlet ( 43 ) of the sorption buffer device ( 40 );
wherein, during a phase (P 2 ) of elevated loading (φ 2 ) of the gas stream (G 1 ) with the sorbable substance, a region (B 1 ) with an elevated loading (ψ) of the sorbent ( 44 ) with the sorbable substance, which region extends from the inlet ( 42 ) of the sorption buffer device ( 40 ) along the sorption path ( 45 ), is formed, and, during a subsequent phase (P 1 ) of reduced loading (φ 1 ) of the gas stream (G 1 ), the region with the elevated loading (ψ) of the sorbent ( 44 ) is shifted along the sorption path ( 45 ) in the direction toward the outlet ( 43 ) of the sorbent buffer device ( 40 ), and
wherein a length (l) of the sorption path ( 45 ) and a quantity of the sorbent ( 44 ) in the sorption buffer device ( 40 ) are selected ( 721 ) in such a way that the sorption buffer device ( 40 ) is set up for accommodating at least three different regions (B 1 -B 5 ) of elevated loading (ψ) of the sorbent ( 44 ) along the sorption path ( 45 ) during the operation of the industrial plant ( 100 ).

2. The method as claimed in claim 1 , further comprising:
expanding ( 731 ) the treated gas stream (G 4 ) with the aid of a pressure reducer ( 50 ) arranged in the outflow direction with respect to the sorption buffer device ( 40 ), wherein an expanded gas stream (G 5 ) is produced; and
feeding ( 732 ) the expanded gas stream (G 5 ) to a gas pipeline ( 60 ) arranged downstream of the sorption buffer device ( 40 ).

3. The method as claimed in claim 2 , wherein a gas pressure difference between the sorption buffer device ( 40 ) and the gas pipeline ( 60 ) is 5 bar-10 bar.

4. The method as claimed in claim 1 , further comprising:
cooling ( 713 ) the laden gas stream (G 1 ) with the aid of a gas-cooling device ( 30 ) arranged upstream of the sorption buffer device ( 40 ), wherein a cooled gas stream (G 3 ) is produced.

5. The method as claimed in claim 4 , wherein the temperature of the cooled gas stream (G 3 ) is 20° C.-50° C.

6. The method as claimed in claim 1 , further comprising compressing ( 712 ) the laden gas stream (G 1 ) with the aid of a compressor ( 20 ), wherein a pressurized gas stream (G 2 ) is produced.

7. The method as claimed in claim 6 , wherein the pressure of the pressurized gas stream (G 2 ) is 20-30 bar.

8. The method as claimed in claim 1 , wherein the adsorption device ( 10 ) comprises a temperature-change adsorption device ( 11 ), a pressure-change adsorption device ( 12 ), or both.

9. The method as claimed in claim 1 , wherein the laden gas stream (G 1 ) comprise(s) gaseous hydrogen, gaseous carbon monoxide, gaseous carbon dioxide, gaseous organic compounds, gaseous water, gaseous nitrogen, gaseous oxygen, a gaseous noble gas, or combinations of these.

10. The method as claimed in claim 9 , wherein the laden gas stream (G 1 ) has a water quantity of 0-4000 ppm by mole, and the treated gas stream (G 4 ) has a water quantity of 500-2000 ppm by mole.

11. The method as claimed in claim 1 , wherein the phase (P 2 ) of elevated loading (φ 2 ) of the laden gas stream (G 1 ) comprises a duration of 2-10 h, and the phase (P 1 ) of reduced loading (φ 1 ) of the laden gas stream (G 1 ) lasts at least twice as long as the phase (P 2 ) of elevated loading (φ 2 ) of the laden gas stream (G 1 ).

12. The method as claimed in claim 1 , wherein the mass flow rate of the laden gas stream (G 1 ) and/or of the treated gas stream (G 4 ) lies between 500 standard m 3 /h and 20 000 standard m 3 /h.

13. An industrial plant for the implementation of the method as claimed in claim 1 , comprising:
the adsorption device ( 10 ) from which the gas stream (G 1 ) laden with a sorbable substance with a predefined mass flow rate is emitted, and the sorption buffer device ( 40 ) to which the laden gas stream (G 1 ) is fed to the inlet ( 42 ) thereof;
wherein a length (l) of a sorption path ( 45 ) and a quantity of a sorbent ( 44 ) in the sorption buffer device ( 40 ) are set up in such a way that the sorption buffer device ( 40 ) is suitable for accommodating the at least three different regions (B 1 -B 5 ) of elevated loading (ψ) of the sorbent ( 44 ) along the sorption path ( 45 ) during the operation of the industrial plant ( 100 ).

14. The industrial plant as claimed in claim 13 , wherein the laden gas stream (G 1 ) is treated in such a way that the treated gas stream (G 4 ) has a reduced loading (φ′ 2 ) in relation to the elevated loading (φ 2 ) of the laden gas stream (G 1 ) and the treated gas stream (G 4 ) has an elevated loading (φ′ 1 ) in relation to the reduced loading (φ 1 ) of the laden gas stream (G 1 ).

15. The method as claimed in claim 1 , wherein the treated gas stream (G 4 ) comprise(s) gaseous hydrogen, gaseous carbon monoxide, gaseous carbon dioxide, gaseous organic compounds, gaseous water, gaseous nitrogen, gaseous oxygen, a gaseous noble gas, or combinations of these.

16. The method as claimed in claim 9 , wherein the treated gas stream (G 4 ) comprise(s) gaseous hydrogen, gaseous carbon monoxide, gaseous carbon dioxide, gaseous organic compounds, gaseous water, gaseous nitrogen, gaseous oxygen, a gaseous noble gas, or combinations of these.

17. The method as claimed in claim 9 , wherein the laden gas stream (G 1 ) has a water quantity of 0-4,000 ppm by mole, and the treated gas stream (G 4 ) has a water quantity of 750-1,500 ppm by mole.

18. The method as claimed in claim 1 , wherein the phase (P 2 ) of elevated loading (φ 2 ) of the laden gas stream (G 1 ) comprises a duration of 2-10 h, and the phase (P 1 ) of reduced loading (φ 1 ) of the laden gas stream (G 1 ) lasts at least three times as long as the phase (P 2 ) of elevated loading (φ 2 ) of the laden gas stream (G 1 ).

19. The method as claimed in claim 1 , wherein the mass flow rate of the laden gas stream (G 1 ) and/or of the treated gas stream (G 4 ) lies between 8,000 standard m 3 /h and 17,000 standard m 3 /h.

20. The method as claimed in claim 1 , wherein the length (l) of the sorption path ( 45 ) and a quantity of the sorbent ( 44 ) in the sorption buffer device ( 40 ) are selected ( 721 ) in such a way that the sorption buffer device ( 40 ) is set up for accommodating at least four different regions (B 1 -B 5 ) of elevated loading (ψ) of the sorbent ( 44 ) along the sorption path ( 45 ) during the operation of the industrial plant ( 100 ).

21. The method as claimed in claim 1 , wherein

Assignees

• Linde Ag

Inventors

• Trott Thomas
• Christian Horn

Classifications

• B01D2257/80

  Water · CPC title

• B01D2257/11

  Noble gases · CPC title

• B01D2256/245

  Methane · CPC title

• B01D2257/104

  Oxygen · CPC title

• B01D2259/40001

  Methods relating to additional, e.g. intermediate, treatment of process gas · CPC title