US2017160010A1PendingUtilityA1

Use of Eductor for Liquid Disposal from Vessel

Individually held — no corporate assignee on recordPriority: Dec 3, 2015Filed: Nov 29, 2016Published: Jun 8, 2017
Est. expiryDec 3, 2035(~9.3 yrs left)· nominal 20-yr term from priority
B01B 1/005F25J 2290/12F25J 2235/60F25J 2205/02F25J 3/08F25J 2235/06C10L 3/101F25J 2240/60C10L 3/06F25J 3/0295F25J 2260/60F25J 2210/12F25J 2245/02F25J 2280/20F25J 1/0022F25J 2215/04F25J 1/0248F25J 3/0219F25J 3/061F25J 3/0209F25J 3/062F25J 3/0695
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Claims

Abstract

A system for the processing of a hydrocarbon flare gas. An input gas stream contains a gas component and a liquid component. A knock-out drum separates the gas component from the liquid component. An eductor has a motive inlet, a suction inlet, and a discharge outlet. The separated liquid component is introduced into the suction inlet of the eductor. A high-pressure gas stream is introduced into the motive inlet of the eductor. The high-pressure gas stream has a pressure sufficient to draw the separated liquid component from the knock-out drum and through the discharge outlet.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
         1 . A system for the processing of a hydrocarbon flare gas, comprising:
 an input gas stream containing a gas component and a liquid component;   a knock-out drum that separates the gas component from the liquid component;   an eductor having a motive inlet, a suction inlet, and a discharge outlet;   wherein the separated liquid component is introduced into the suction inlet of the eductor; and   a high-pressure gas stream introduced into the motive inlet of the eductor, the high-pressure gas stream having a pressure sufficient to draw the separated liquid component from the knock-out drum and through the discharge outlet.   
     
     
         2 . The system of  claim 1 , wherein the knock-out drum has a boot or sump, and wherein the separated liquid component is drawn from the boot or sump to the suction inlet of the eductor. 
     
     
         3 . The system of  claim 1 , wherein the high-pressure gas stream is a defrost gas stream. 
     
     
         4 . The system of  claim 1 , wherein the high-pressure gas stream has a pressure of about 100 psig and the input gas stream has a pressure between 1-2 psig. 
     
     
         5 . The system of  claim 1 , further comprising a dry flare that flares the gas component of the input gas stream after the liquid component has been separated therefrom in the knock-out drum. 
     
     
         6 . A cryogenic or cold gas processing system, comprising:
 an input gas stream containing a gas component and a liquid component;   a knock-out drum that separates the gas component from the liquid component, the knock-out drum having a fluid outlet through which the separated liquid component exits the knock-out drum;   a flare that flares the gas component of the input gas stream after the liquid component has been separated therefrom in the knock-out drum;   an eductor having a motive inlet, a suction inlet, and a discharge outlet;   wherein the separated liquid component is introduced from the fluid outlet to the suction inlet of the eductor; and   a high-pressure gas stream introduced into the motive inlet of the eductor, the high-pressure gas stream having a pressure sufficient to draw the separated liquid component from the knock-out drum and through the discharge outlet.   
     
     
         7 . The system of  claim 6 , wherein the high-pressure gas stream is a defrost gas stream. 
     
     
         8 . The system of  claim 6 , wherein the high-pressure gas stream has a pressure of about 100 psig and the input gas stream has a pressure between 1-2 psig.

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