Liquid-gas contacting apparatus and pump therefor

Claim 2

A glycol dehydrator, comprising a contacting vessel having a gas inlet, a gas outlet, a lean glycol inlet, a wet glycol outlet and means within said vessel for providing contact between the gas and the glycol flowing therethrough, a glycol regenerator, a first time communicating between the wet glycol outlet and the glycol regenerator, a second line communicating between the regenerator and the lean glycol inlet, a gear motor in said first line, a gear pump in said second line, means connecting said motor to said pump whereby wet glycol and gas from said contacting vessel provides sufficient power to drive said pump to pump lean glycol into said contacting vessel, a gas fired burner in contact with said glycol regenerator, means in said first line between said gear motor and the regenerator for separating gas from wet glycol discharged from said gear motor, and means for delivering said separated gas to said burner to provide at least a portion of the gas to fire said regenerator burner.

Claim 3

A glycol dehydrator comprising a contacting vessel having a gas inlet, a gas outlet, a lean glycol inlet, a wet glycol outlet and means within said vessel for providing contact between the gas and the glycol flowing therethrough, a glycol regenerator having a wet glycol inlet, a lean glycol outlet and a burner to heat the glycol within the regenerator whereby water in the wet glycol is vaporized to provide a lean glycol, a first line connecting from the wet glycol outlet of said contacting vessel to the wet glycol inlet of said glycol regenerator, a second line connecting from the lean glycol outlet of said regenerator to the lean glycol inlet of said contacting vessel, a gear motor in said first line to be powered by fluids flowing therethrough, a liquid-gas separator in said first line between said gear motor and said glycol regenerator and having a fluid inlet connected to the portion of said first line leading from said motor, a glycol outlet connected to the portion of said first line leading to said regenerator and a gas outlet connected to said burner, a gear pump in said second line to pump lean glycol from said regenerator to said contacting vessel, a flow control means in said second line downstream of said gear pump to control the rate of flow of lean glycol to said contacting vessel, and means connecting said motor to said pump whereby wet glycol and gas from said contacting vessel provides sufficient power to drive said pump to pump lean glycol into said contacting vessel, said motor having a greater volumetric capacity than said pump to allow sufficient gas to pass therethrough with the wet glycol to assure continuous flow of lean glycol at a preselected flow rate to said contacting vessel.

Claim 4

A glycol dehydrator comprising a contacting vessel having a gas inlet, a gas outlet, a lean glycol inlet, a wet glycol outlet and means within said vessel for providing contact between the gas and the glycol flowing therethrough, a glycol regenerator having a wet glycol inlet, a lean glycol outlet and a burner to heat the glycol within the regenerator whereby water in the wet glycol is vaporized to provide a lean glycol, a first line connecting from the wet glycol outlet of said contacting vessel to the wet glycol inlet of said glycol regenerator, a second line connecting from the lean glycol outlet of said regenerator to the lean glycol inlet of said contacting vessel, a gear motor in said first line to be powered by fluids flowing therethrough, a liquid-gas separator in said first line between said gear motor and said glycol regenerator and having a fluid inlet connected to the portion of said first line leading from said motor, a glycol outlet connected to the portion of said first line leading to said regenerator and a gas outlet connected to said burner, a gear pump in said second line to pump lean glycol from said regenerator to said contacting vessel, a flow control means in said second line downstream of said gear pump to control the rate of flow of lean glycol to said contacting vessel, and means connecting said motor to said pump whereby wet glycol and gas from said contacting vessel provides sufficient power to drive said pump to pump lean glycol into said contacting vessel, said motor having a greater volumetric capacity than said pump to allow sufficient gas to pass therethrough with the wet glycol to assure continuous flow of lean glycol at a preselected flow rate to said contacting vessel.

Claim 5

In a glycol dehydrator having, a contacting vessel with a gas inlet and wet glycol outlet, and a gas outlet and lean glycol inlet; and a glycol regenerator, a first flow line from the glycol regenerator to said lean glycol inlet to provide lean glycol to said vessel, and a second flow line from said wet glycol outlet and vessel in fluid communication with said regenerator to receive wet glycol and gas from the vessel and provide wet glycol to the regenerator for recirculation of the glycol; the improvement of a glycol pump structure between said vessel and said regenerator comprising: a positive displacement rotary gear pump in said first flow line between said vessel and said regenerator to provide during operation a continuous uninterrupted flow of lean glycol to said vessel; a positive displacement rotary gear motor in said second flow line between said vessel and said regenerator to provide during operation a continuous flow of wet glycol and gas from said vessel to said regenerator; and drive means connecting said rotary motor to said rotary pump whereby wet glycol and gas from said contacting vessel to said rotary motor provides sufficient power for said rotary motor to drive said rotary pump for pumping lean glycol into said contacting vessel; said rotary gear motor having a greater volumetric capacity than said rotary gear pump thereby permitting sufficient gas to pass through the rotary motor with the wet glycol to assure a continuous flow of lean glycol from the rotary pump to said contacting vessel at a preselected flow rate.

Claim 6

In a glycol dehydrator having, a contacting vessel with a gas inlet and wet glycol outlet, and a gas outlet and lean glycol inlet; and a glycol regenerator, a first flow line from the glycol regenerator to said lean glycol inlet to provide lean glycol to said vessel, and a second flow line from said wet glycol outlet and vessel in fluid communication with said regenerator to receive wet glycol and gas from the vessel and provide wet glycol to the regenerator for recirculation of the glycol; the improvement of a glycol pump structure between said vessel and said regenerator comprising: a positive displacement rotary gear pump in said first flow line between said vessel and said regenerator to provide during operation a continuous uninterrupted flow of lean glycol to said vessel; a positive displacement rotary gear motor in said second flow line between said vessel and said regenerator to provide during operation a continuous flow of wet glycol and gas from said vessel to said regenerator; and drive means connecting said rotary motor to said rotary pump whereby wet glycol and gas from said contacting vessel to said rotary motor provides sufficient power for said rotary motor to drive said rotary pump for pumping lean glycol into said contacting vessel; said rotary gear motor having a greater volumetric capacity than said rotary gear pump thereby permitting sufficient gas to pass through the rotary motor with the wet glycol to assure a continuous flow of lean glycol from the rotary pump to said contacting vessel at a preselected flow rate.

Claim 7

The glycol dehydrator as set forth in claim 3 wherein said rotary gear motor has a volumetric capacity in the range of 1.2 to 2.0 times the volumetric capacity of said rotary gear pump.