METHODS AND SYSTEMS FOR CONTROLLING CONDENSATE WHEN REDUCING OXYGEN CONTENT IN BIOGAS
A method of neutralizing condensate from a gas flow subject to a combustion oxygen removal process passing through a number of cooling steps post combustion includes: providing a supply of water to the gas flow prior to a particular cooling step of the number of cooling steps; collecting an aqueous condensate solution from the gas flow prior to the particular cooling step; and providing a supply of a neutralizing agent to the aqueous condensate solution.
1 . A method of neutralizing condensate from a gas flow subject to a combustion oxygen removal process passing through a number of cooling steps post combustion, the method comprising:
providing a supply of water to the gas flow prior to a particular cooling step of the number of cooling steps;
collecting an aqueous condensate solution from the gas flow prior to the particular cooling step; and
providing a supply of a neutralizing agent to the aqueous condensate solution.
2 . The method of claim 1 , wherein providing the supply of the neutralizing agent to the aqueous condensate solution comprises providing a supply of an aqueous neutralizing agent.
3 . The method of claim 1 , wherein the number of cooling steps comprises a plurality of cooling steps in series, and wherein the method further comprises, prior to providing the supply of water to the gas flow, determining as the particular cooling step a cooling step among the plurality of colling steps in which liquid condensate occurs from the gas flow.
4 . The method of claim 3 , wherein determining the cooling step in which liquid condensate occurs from the gas flow comprises:
determining the temperature achieved at the different points along the plurality of cooling steps as well as a vapor pressure of the water associated with the temperatures at each point;
determining a partial pressure of the water in gaseous phase post reaction using inlet water concentration in addition to the stoichiometric amount of water created from the combustion of the oxygen present with the methane and using the thermodynamic properties of the system and
determining a location where the vapor pressure of the water becomes equal to the partial pressure of the water.
5 . The method of claim 1 , wherein providing the supply of water to the gas flow prior to the particular cooling step comprises providing a continuous supply of water to the gas flow via an inserted atomizing lance.
6 . The method of claim 1 , wherein:
providing the supply of water to the gas flow prior to the particular cooling step comprises providing the supply of water within process piping carrying the gas flow, and
collecting the aqueous condensate solution from the gas flow prior to the particular cooling step comprises collecting the aqueous condensate solution from the process piping.
7 . The method of claim 1 , wherein:
providing the supply of water to the gas flow prior to the particular cooling step comprises providing the supply of water within a gas-liquid contact tower, and
collecting the aqueous condensate solution from the gas flow prior to the particular cooling step comprises collecting the aqueous condensate solution from the contact tower.
8 . The method of claim 2 , wherein providing the supply of the aqueous neutralizing agent comprises providing the aqueous neutralizing agent via an inserted atomizing lance.
9 . The method of claim 1 , wherein the neutralizing agent is a NaOH solution.
10 . The method of claim 1 , further comprising communicating a remaining gas flow from the gas flow after providing the supply of water to the particular cooling step.
11 . The method of claim 1 , wherein the particular cooling step comprises one of:
a gas-gas economizing exchanger,
an air-cooling heat exchanger, or
a refrigeration-based cooling heat exchanger.