Natural gas conditioning system and method

Claim 2

In a method for conditioning natural gas from a gas well, said method including expanding the gas to separate liquid water and condensible hydrocarbons therefrom, contacting the resulting wet gas with a liquid dessicant which absorbs water vapor from the wet gas and heating the liquid dessicant to drive off water therefrom, the improvement comprising maintaining the temperature of the expanding gas within a preselected range by controllably heating the gas prior to expansion by heat exchange with heated dessicant from the dessicant-heating step in response to the temperature of the expanding gas.

Claim 3

A method as in claim 1 wherein the step of controllably heating the gas includes passing the gas in heat exchange relationship with the heated dessicant and bypassing the heat exchange relationship so as to pass unheated gas to the separating step in accordance with a preselected high temperature of the gas in the separating step.

Claim 4

In a method of conditioning natural gas: expanding the gas and removing therefrom the resulting liquid water and condensed liquid hydrocarbons and dehydrating the resulting wet gas by spraying strong liquid dessicant into a stream of the wet gas thereby forming a gas/liquid stream in which the gas and liquid are in co-current contact with each other, introducing the gas/liquid stream into the lower portion of a bed of gas-liquid contact material and passing the gas and dessicant upwardly in the bed in co-current contact, removing weak dessicant from the bed above the location at which the gas/liquid stream is introduced, introducing additional strong liquid dessicant into the upper portion of the bed and passing the thus introduced dessicant downwardly in the upper portion of the bed in counter-current contact with the gas passing upwardly from the lower portion of the bed.

Claim 5

In a method of conditioning natural gas: expanding the gas and removing therefrom the resulting liquid water and condensed liquid hydrocarbons and dehydrating the resulting wet gas by spraying strong liquid dessicant into a stream of the wet gas thereby forming a gas/liquid stream in which the gas and liquid are in co-current contact with each other, introducing the gas/liquid stream into the lower portion of a bed of gas-liquid contact material and passing the gas and dessicant upwardly in the bed in co-current contact, removing weak dessicant from the bed above the location at which the gas/liquid stream is introduced, introducing additional strong liquid dessicant into the upper portion of the bed and passing the thus introduced dessicant downwardly in the upper portion of the bed in counter-current contact with the gas passing upwardly from the lower portion of the bed.

Claim 6

In apparatus for conditioning natural gas from a gas well including a separator in which the gas is expanded through a choke into a separator space and from which liquid water and condensed liquid hydrocarbons are removed, a dehydrator in which wet gas from the separator is contacted with a liquid dessicant which absorbs water vapor from the wet gas, and a reboiler for heating the liquid dessicant from the dehydrator to drive off water from the dessicant: heat exchange means for heating well gas before the gas passes through said choke o said separator space; and control means responsive to the temperature in said separator space for controlling the flow of gas through said heat exchange means to thereby control the temperature in said separator space.

Claim 7

In apparatus for conditioning natural gas from a gas well including a separator in which the gas is expanded through a choke into a separator space and from which liquid water and condensed liquid hydrocarbons are removed, a dehydrator in which wet gas from the separator is contacted with a liquid dessicant which absorbs water vapor from the wet gas, and a reboiler for heating the liquid dessicant from the dehydrator to drive off water from the dessicant: heat exchange means for heating well gas before the gas passes through said choke o said separator space; and control means responsive to the temperature in said separator space for controlling the flow of gas through said heat exchange means to thereby control the temperature in said separator space.

Claim 8

Apparatus as in claim 4 wherein said heat exchange means is arranged to pass well gas in heat exchange relationship with hot liquid dessicant from the reboiler and wherein said control means includes a temperature sensor for sensing the temperature of the gas expanding in said separator and a bypass assembly controlled by said sensor for passing at least a portion of the well gas through said heat exchanger in response to a predetermined low temperature in said separator and for bypassing said heat exchanger in response to a predetermined higher temperature in said separator.

Claim 9

Apparatus as in claim 4 including a gas-fired heater in said reboiler, a storage tank connected to said reboiler to receive hot liquid dessicant therefrom and second heat exchange means in association with liquid dessicant in said storage tank for passing warm liquid dessicant from said dehydrator in heat exchange relationship with the hot dessicant in said storage tank before the dessicant from said dehydrator passes to said reboiler, whereby the dessicant from said dehydrator is preheated and the temperature of the dessicant in said storage tank is reduced, said well-gas heat exchange means being arranged to pass the well gas in heat exchange relationship with dessicant in said storage tank thereby extracting additional heat from the dessicant in said storage tank.

Claim 10

In apparatus for conditioning natural gas from a gas well, of the type including a separator in which the gas is expanded to separate liquid water and condensible hydrocarbons therefrom; a dehydrator in which wet gas from the separator is contacted with a liquid dessicant which absorbs water vapor from the wet gas and a reboiler for heating weak liquid dessicant from the dehydrator to drive off water to form strong dessicant, an improved dehydrator having a first contacting stage comprising an inner generally vertical conduit having an open upper end and a lower end in communication with said separator so as to conduct wet gas from said separator, an outer generally vertical conduit surrounding said inner conduit, said outer conduit having a closed upper end located above the open upper end of said inner conduit and an open lower end, means for introducing strong liquid dessicant into the upper end of said outer conduit whereby the introduced dessicant and the gas issuing from the upper end of said inner conduit pass downwardly in contact with each other through said outer conduit; and a second dehydrator stage comprising a column of gas/liquid packing material surrounding said outer conduit of said first dehydrator stage and having a lower end portion in communication with the open lower end of said outer conduit so that gas and liquid dessicant issuing therefrom pass upwardly in said column of packing material, means for introducing strong liquid dessicant into the upper portion of said column of packing material and means for removing weak liquid dessicant from said column of packing material at a location intermediate the upper and lower portions of said column.

Claim 11

In apparatus for conditioning natural gas from a gas well, of the type including a separator in which the gas is expanded to separate liquid water and condensible hydrocarbons therefrom; a dehydrator in which wet gas from the separator is contacted with a liquid dessicant which absorbs water vapor from the wet gas and a reboiler for heating weak liquid dessicant from the dehydrator to drive off water to form strong dessicant, an improved dehydrator having a first contacting stage comprising an inner generally vertical conduit having an open upper end and a lower end in communication with said separator so as to conduct wet gas from said separator, an outer generally vertical conduit surrounding said inner conduit, said outer conduit having a closed upper end located above the open upper end of said inner conduit and an open lower end, means for introducing strong liquid dessicant into the upper end of said outer conduit whereby the introduced dessicant and the gas issuing from the upper end of said inner conduit pass downwardly in contact with each other through said outer conduit; and a second dehydrator stage comprising a column of gas/liquid packing material surrounding said outer conduit of said first dehydrator stage and having a lower end portion in communication with the open lower end of said outer conduit so that gas and liquid dessicant issuing therefrom pass upwardly in said column of packing material, means for introducing strong liquid dessicant into the upper portion of said column of packing material and means for removing weak liquid dessicant from said column of packing material at a location intermediate the upper and lower portions of said column.

Claim 12

In a separator-dehydrator for conditioning natural gas: an elongated vessel having a separation stage in one end for expanding the gas and removing the resulting liquid water and condensed hydrocarbons; at least one dehydration stage in said vessel adjacent the separation stage for contacting the wet gas from the separation stage with strong liquid dessicant, said dehydration stage comprising conduit means for conducting wet gas from said separation stage, means for spraying strong liquid dessicant into said conduit means so as to effect contact of the gas passing therethrough with droplets of the dessicant, a bed of gas/liquid contact material in said vessel, means for passing the resulting gas-dessicant mixture into the lower portion of the bed of contact material, means for introducing additional strong liquid dessicant into the upper portion of the bed of contact material, means for removing weak dessicant from the bed at a location between the upper and lower portions of the bed and means for removing dry gas from said vessel.

Claim 13

In a separator-dehydrator for conditioning natural gas: an elongated vessel having a separation stage in one end for expanding the gas and removing the resulting liquid water and condensed hydrocarbons; at least one dehydration stage in said vessel adjacent the separation stage for contacting the wet gas from the separation stage with strong liquid dessicant, said dehydration stage comprising conduit means for conducting wet gas from said separation stage, means for spraying strong liquid dessicant into said conduit means so as to effect contact of the gas passing therethrough with droplets of the dessicant, a bed of gas/liquid contact material in said vessel, means for passing the resulting gas-dessicant mixture into the lower portion of the bed of contact material, means for introducing additional strong liquid dessicant into the upper portion of the bed of contact material, means for removing weak dessicant from the bed at a location between the upper and lower portions of the bed and means for removing dry gas from said vessel.

Claim 14

Apparatus for conditioning natural gas from a gas well comprising: a vertically-elongated separator-dehydrator vessel having therein a lower separating space into which well gas is expanded through a choke and an upper dehydrating space in which wet gas from said separating space is passed in contact with a warm strong liquid dessicant which absorbs water vapor from the wet gas; a dessicant reboiler vessel heated by a well gas burner; a dessicant storage tank for receiving strong hot dessicant from said reboiler; first and second heat exchange means in said storage tank; means for passing weak liquid dessicant from said separator space after contact with wet gas to said reboiler via said first heat exchange means thereby extracting heat from the liquid dessicant in said storage tank; a temperature sensor in said separating space of said separator-dehydrator vessel for sensing the temperature of gas expanding in said space; means for selectively passing gas from the well either directly to said choke or through said second heat exchange means and then to said choke in response to a predetermined low temperature of gas expanding in said separator space thereby controlling the temperature of the expanding gas; and means for passing warm strong dessicant from said storage tank to said dehydrator space in said separator-dehydrator vessel.

Claim 15

Apparatus for conditioning natural gas from a gas well comprising: a vertically-elongated separator-dehydrator vessel having therein a lower separating space into which well gas is expanded through a choke and an upper dehydrating space in which wet gas from said separating space is passed in contact with a warm strong liquid dessicant which absorbs water vapor from the wet gas; a dessicant reboiler vessel heated by a well gas burner; a dessicant storage tank for receiving strong hot dessicant from said reboiler; first and second heat exchange means in said storage tank; means for passing weak liquid dessicant from said separator space after contact with wet gas to said reboiler via said first heat exchange means thereby extracting heat from the liquid dessicant in said storage tank; a temperature sensor in said separating space of said separator-dehydrator vessel for sensing the temperature of gas expanding in said space; means for selectively passing gas from the well either directly to said choke or through said second heat exchange means and then to said choke in response to a predetermined low temperature of gas expanding in said separator space thereby controlling the temperature of the expanding gas; and means for passing warm strong dessicant from said storage tank to said dehydrator space in said separator-dehydrator vessel.

Claim 16

Apparatus as in claim 9 wherein said dehydrator space includes a first contacting stage comprising an inner generally vertical conduit having an open upper end and a lower end in communication with said separating space so as to conduct wet gas from said separating space, an outer generally vertical conduit surrounding said inner conduit, said outer conduit having a closed upper end located above the open upper end of said inner conduit and an open lower end, said means for passing warm strong liquid dessicant introducing said dessicant into the upper end of said outer conduit whereby the introduced dessicant and the gas issuing from the upper end of said inner conduit pass downwardly in contact with each other through said outer conduit; and a second dehydrator stage comprising a column of gas/liquid packing material surrounding said outer conduit of said first dehydrator stage and having a lower end portion in communication with the open lower end of said outer conduit so that gas and liquid dessicant issuing therefrom pass upwardly in said column of packing material, said means for passing warm strong liquid dessicant also introducing said dessicant into the upper portion of said column of packing material and means for removing weak liquid dessicant from said column of packing material at a location intermediate the upper and lower portions of said column.

Claim 17

Apparatus for conditioning natural gas from a gas well comprising: a separator in which the gas is expanded; a dehydrator in which wet gas from said separator is passed in contact with a warm strong liquid dessicant which absorbs water vapor from the wet gas; a dessicant reboiler vessel heated by a well gas burner; a dessicant storage tank for receiving strong hot dessicant from said reboiler; first and second heat exchange means in said storage tank; means for passing weak liquid dessicant from said separator after contact with wet gas to said reboiler via said first heat excahnge means thereby extracting heat from the liquid dessicant in said storage tank; and means for selectively passing gas from the well either directly to said separator or through said second heat exchange means and then to said separator thereby controlling the temperature of the expanding gas; and means for passing warm strong dessicant from said storage tank to said dehydrator.

Claim 18

Apparatus for conditioning natural gas from a gas well comprising: a separator in which the gas is expanded; a dehydrator in which wet gas from said separator is passed in contact with a warm strong liquid dessicant which absorbs water vapor from the wet gas; a dessicant reboiler vessel heated by a well gas burner; a dessicant storage tank for receiving strong hot dessicant from said reboiler; first and second heat exchange means in said storage tank; means for passing weak liquid dessicant from said separator after contact with wet gas to said reboiler via said first heat excahnge means thereby extracting heat from the liquid dessicant in said storage tank; and means for selectively passing gas from the well either directly to said separator or through said second heat exchange means and then to said separator thereby controlling the temperature of the expanding gas; and means for passing warm strong dessicant from said storage tank to said dehydrator.