Gas-To-Liquids Conversion Process Using Electron-Beam Irradiation

Abstract

A process for converting light alkanes from a natural gas production stream to higher molecular weight hydrocarbons is provided. The method includes transporting the natural gas stream to an electron beam reactor, such as a steel flow-type radiation reactor connected hermetically to an accelerator beam window. The gas stream is exposed to electron beam radiation to generate an upgraded and substantially liquefied hydrocarbon stream. The method then includes transporting the substantially liquefied hydrocarbon stream into a scrubber to remove non-condensed gases. The remaining liquid hydrocarbon stream is then transported as condensate to a distillation tower, where high octane products are separated through fractionation.

1 . A process for converting a gas stream comprising primarily a mixture of light alkanes into a high-octane liquid stream, comprising: transporting the gas stream to a reactor at a gas processing facility; introducing the gas stream into a reactor whereupon components of the gas stream are exposed to electron beam radiation within the reactor to increase the molecular weight of hydrocarbons in the gas stream, thereby producing an upgraded radiolysis fluid stream; transporting the radiolysis fluid stream into a separator; re-circulating the first stream back into an inlet of the reactor for additional irradiation and upgrading; and transporting the liquid stream off-site for further processing or for commercial sale. 
     
     
         2 . The process of  claim 1 , wherein the gas stream is a natural gas stream, an artificial gaseous alkane mixture, or gaseous industrial waste. 
     
     
         3 . The process of  claim 1 , wherein: the gas stream originates from a natural gas stream incident to oil and gas production operations; and transporting the natural gas stream to a reactor comprises moving the natural gas stream from a wellhead or from a field gathering facility to the reactor. 
     
     
         4 . The process of  claim 1 , further comprising: (i) removing any H2O from the natural gas stream before introducing the natural gas stream into the reactor, (ii) removing any CO2 from the natural gas stream before introducing the natural gas stream into the reactor, (ii) removing any H2S from the natural gas stream before introducing the natural gas stream into the reactor, or (iii) combinations thereof. 
     
     
         5 . The process of  claim 1 , further comprising: pressuring the natural gas stream to at least 15 psi, and heating the natural gas stream to at least 100.degree. F. before introducing the natural gas stream into the reactor. 
     
     
         6 . The process of  claim 1 , wherein pressuring and heating the natural gas production stream is done through the use of at least one blower. 
     
     
         7 . The process of  claim 1 , wherein the separate comprises one or more gas-liquid centrifugal separators in series. 
     
     
         8 . The process of  claim 1 , further comprising: monitoring the hydrogen (H.sub.2) content in the first gaseous stream released from the separator; and when the hydrogen content reaches 100/% by volume in the first gaseous stream, sending non-condensed gases of the first gaseous stream to a hydrogen separator for removal of hydrogen gases before the first gaseous stream is re-circulated back into the reactor for additional irradiation and upgrading. 
     
     
         9 . The process of  claim 1 , wherein: excess hydrogen is removed from the non-condensed gases by a pressure swing absorption unit; and the pressure swing absorption unit is operated at 100 psi and contains (i) activated carbon, (ii) zeolite, or (iii) a combination thereof. 
     
     
         10 . The process of  claim 1 , wherein the pressure swing absorption unit is maintained at 120.degree. F. or higher. 
     
     
         11 . The process of  claim 1 , further comprising: before re-circulating, removing hydrogen gas from the first gaseous stream using a membrane separator. 
     
     
         12 . The process of claim  18 , wherein: the gas production stream is moved through an irradiation area within the reactor at a rate of 800 m.sup.3/hour; and a rate of energy consumption for an absorbed dose rate is 2.0 kW/m.sup.3. 
     
     
         13 . The process of  claim 1 , further comprising: blending at least a portion of the liquid stream as a condensate product into a lower-octane fuel to generate a higher-octane transportation fuel.