公开(公告)号：US10076721B2

公开(公告)日：2018-09-18

申请号：US15407561

申请日：2017-01-17

Applicant: Chevron U.S.A. Inc.

Inventor： Saham Sam Tafreshi ,  Kamal Gursahani ,  Yawen Q. Owen ,  Robert E. Marshall

IPC: B01D53/26 ,  B01D53/04

CPC classification number: B01D53/261 ,  B01D2253/116 ,  B01D2257/80 ,  B01D2259/4009 ,  C10L3/106 ,  C10L2290/542

Abstract: Water saturated molecular sieve in a gas dehydration unit is regenerated. A short loop is used in which regeneration gas is recycled to a heater upstream of a vessel in regeneration mode. The regeneration gas passes over the molecular sieve in the vessel to desorb water thereby regenerating the molecular sieve. The short loop also includes a condenser, a water separator and a compressor. The regeneration gas is not recycled to the AGRU at the front-end of the plant, thus the regeneration gas flow rate can be increased, as it is not limited by the front-end capacity of the plant. Moreover, the pressure of the system during regeneration can be reduced within the limits of system hydraulics. By using the short loop, the total time required for regeneration can also be reduced. The embodiments disclosed can de-bottleneck molecular sieve regeneration constraints in LNG, LPG or cryogenic gas plants.

公开(公告)号：US20180200664A1

公开(公告)日：2018-07-19

申请号：US15407561

申请日：2017-01-17

Applicant: Chevron U.S.A. Inc.

Inventor： Saham Sam Tafreshi ,  Kamal Gursahani ,  Yawen Q. Owen ,  Robert E. Marshall

IPC: B01D53/04 ,  B01D53/26

CPC classification number: B01D53/0438 ,  B01D53/261 ,  B01D2253/116 ,  B01D2257/80 ,  B01D2259/4009

Abstract: Water saturated molecular sieve in a gas dehydration unit is regenerated. A short loop is used in which regeneration gas is recycled to a heater upstream of a vessel in regeneration mode. The regeneration gas passes over the molecular sieve in the vessel to desorb water thereby regenerating the molecular sieve. The short loop also includes a condenser, a water separator and a compressor. The regeneration gas is not recycled to the AGRU at the front-end of the plant, thus the regeneration gas flow rate can be increased, as it is not limited by the front-end capacity of the plant. Moreover, the pressure of the system during regeneration can be reduced within the limits of system hydraulics. By using the short loop, the total time required for regeneration can also be reduced. The embodiments disclosed can de-bottleneck molecular sieve regeneration constraints in LNG, LPG or cryogenic gas plants.