US2017089809A1PendingUtilityA1

Speed Loop for Take-Off and Return by Single Pipeline Probe

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Assignee: MUSTANG SAMPLING LLCPriority: Sep 30, 2015Filed: Aug 31, 2016Published: Mar 30, 2017
Est. expirySep 30, 2035(~9.2 yrs left)· nominal 20-yr term from priority
G01N 1/44G01N 1/2035G01N 1/14G01N 1/24G01N 1/10G01N 1/02G01N 2001/105G01N 1/2247G01N 1/42G01N 1/22G01N 33/0011G01N 33/225G01N 2001/2064
55
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Claims

Abstract

A post-probe upstream metering pump for insuring phase change completion of a multi-phase fluid such as Natural Gas Liquid (NGL) in a sample conditioning system having a pipeline sample take-off probe for fluid extraction, a sample conditioning unit for conditioning the extracted fluid to a select range of temperature and pressure for analysis of the fluid sample by an associated analyzer without dew point dropout or phase separation, and a metering pump disposed in-line between the sample take-off probe and the sample conditioning unit to pressurize the fluid sample to condense into a substantially fully liquid phase and to reduce lag time between extraction and fluid sample conditioning.

Claims

exact text as granted — not AI-modified
We claim: 
     
         1 . A system for multi-phase fluid sample extraction, comprising:
 a) a sample take-off probe for extracting multi-phase fluid from a pipeline;   b) a sample conditioning unit for vaporizing the extracted fluid sample and maintaining the vaporized sample in select temperature and pressure ranges to prevent dew point dropout and passing the conditioned vaporized sample to a downstream analyzer; and   c) a metering pump disposed in-line between the sample take-off probe and the sample conditioning unit to increase pressure on and condense the extracted fluid sample to maximize transition of the multi-phase fluid sample into a single fully liquid phase.   
     
     
         2 . The system of  claim 1  further comprising a particulate coalescing filter disposed in-line between the sample take-off probe and the metering pump. 
     
     
         3 . The system of  claim 2  where the metering pump is a pneumatic pump. 
     
     
         4 . The system of  claim 3  where the pneumatic pump includes a pneumatic controller and an air isolation valve. 
     
     
         5 . The system of  claim 4  where the pneumatic controller includes at least one feedback sensor. 
     
     
         6 . The system of  claim 1  where the multi-phase fluid is natural gas liquid and further including a speed loop return to the pipeline. 
     
     
         7 . The system of  claim 6  where the metering pump generates a pressure of at least 400 PSIG. 
     
     
         8 . The system of  claim 6  where the metering pump generates pressure of at least 600 PSIG for reinjection of the pressurized, liquid natural gas liquid through the speed loop into the pipeline to overcome suction pressure therefrom. 
     
     
         9 . The system of  claim 1  where the metering pump minimizes lag time from sample extraction to sample conditioning. 
     
     
         10 . The system of  claim 1  further comprising a filter member disposed in-line between the metering pump and the sample conditioning unit where said filter member includes a liquid bypass passage connected to a pipeline sample reinjection return speed loop. 
     
     
         11 . The system of  claim 10  further comprising a fluid flow regulator valve disposed in line between the filtered member and the sample conditioning unit. 
     
     
         12 . The system of  claim 10  further comprising a pipeline reinjection port and where the metering pump generates pressure of at least 600 PSIG to provide for reinjection of pressurized, liquid natural gas liquid through the return speed loop into the pipeline through said reinjection port. 
     
     
         13 . The system of  claim 12  further comprising a flow meter disposed in-line between said liquid bypass and said reinjection port to measure a flow rate of the sample liquid passing therethrough. 
     
     
         14 . The system of  claim 12  further comprising a back pressure regulator disposed in-line between said liquid bypass and said reinjection port to prevent liquid backflow into said filter member. 
     
     
         15 . The system of  claim 1  further including a speed loop return to the pipeline and where the multi-phase fluid is natural gas liquid and the metering pump generates pressure of at least 600 PSIG for reinjection of the pressurized, liquid natural gas liquid through the speed loop into the pipeline to overcome suction pressure therefrom. 
     
     
         16 . A method for maximizing single state liquid sample of natural gas liquid extracted by means of a pipeline sample take-off probe prior to vaporization for analysis using the metering pump, comprising the steps of:
 a) extracting a natural gas liquid fluid sample from a pipeline process stream through a sample take-off probe;   b) pressurizing the extracted sample fluid to maximize complete condensation into a liquid phase; and   c) communicating the pressurized liquid sample to a sample conditioner for vaporizing the liquid sample for passage from the sample conditioner to a downstream analyzer at a select pressure and temperature to minimize phase change.   
     
     
         17 . The method of  claim 16  where the system includes a coalescent filter element disposed between the sample take-off probe and the metering pump further comprising the step of passing the sample through the coalescent filter element to minimize passage of vapor and entrained gases contained in the multi-phase natural gas liquid to the metering pump. 
     
     
         18 . The method of  claim 17  where the system includes a liquid bypass, a pipeline sample return speed loop, and a pipeline reinjection port where the metering pump pressurizes the extracted sample to at least 600 PSIG to provide for reinjection of pressurized, liquid natural gas liquid sample through the pipeline reinjection port. 
     
     
         19 . The method of  claim 18  where the liquid bypass is filtered and the return speed loop includes an in-line back pressure regulating valve, the method further comprising the step of minimizing phase change from the liquid state of pressurized, liquid natural gas liquid sample passing through the filtered bypass and to the reinjection port. 
     
     
         20 . The method of  claim 19  further comprising the step of minimizing lag time between sample extraction and extracted sample vaporization.

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