New & Refurbished TEG Units
As a refurbisher of glycol units, Croft has seen decades of units used under varying conditions and has developed a testing and inspection plan for areas of concern and additions and changes that are incorporated into different designs to give optimal performance.
As a new manufacturer of glycol units, we have taken the optimal design choices across many units and improved trouble areas to provide robust and operator-friendly units.
The components included on our standard glycol units are typically options from other manufacturers. We believe certain features are required for a properly functioning unit and our goal is to minimize operational issues while exceeding performance requirements.
We have numerous upgrade options as well for the units such as BTEX units for emissions elimination, Burner Management Systems for exceptional process control and reliability, and safety devices to protect pumps from costly rebuilds.
We can also customize the units to our client requirements with whatever equipment required up to and exceeding 14C requirements.
Many pipelines or gathering systems require the removal of water vapor from natural gas, also known as dehydration. This dehydration or water dewpoint reduction of the gas reduces corrosion in pipelines and prevents the formation of hydrates that can block pipelines.
The most common method of dehydrating natural gas in the field is by using a glycol dehydrator or TEG unit. This method of dehydration typically utilizes Tri-ethylene Glycol (TEG) to absorb the water vapor from the natural gas and then regenerate the glycol for continuous reuse in the unit. Standard units are designed to meet a water content outlet specification of less than 7 lbs./MMcf but an upgraded unit can meet specifications of less than 3 lbs./MMcf.
How it Works
A glycol unit is comprised of two major components, the contact tower, and the regeneration skid. Gas enters the bottom of the contact tower, also known as an absorber, at the same time lean glycol is pumped into the top of the tower. The gas contacts the glycol through special internals in the tower to facilitate the absorption of the water vapor. Typical glycol tower internals are chosen depending on the parameters of the application and tower sizing required. Once the glycol reaches the bottom of the tower it is sent to the regeneration skid to remove the absorbed water. The glycol will be run through separation to remove gas and oils it may have picked up and then filtered. It will then be heated through heat exchangers and enter the reboiler still column where it will be heated to 375-400*F to boil the water out of the glycol. After the reboiler, it is pumped back to the contact tower to continue the regenerative process.
Sizing of a glycol unit is based on determining the correct contact tower to pair with a regeneration skid.
The contact tower size is based on the Volume, Pressure, Internals Used, water contact entering the unit, and the outlet water content required. Random packing is used for smaller diameter towers typically under 20” Diameter. Bubble cap trays are the most common and typically used for 20”-60” diameter towers and contain from 6-10 trays depending on application parameters. Structured Packing is typically used on larger volume applications and can handle higher volumes than bubble caps with the same diameter tower.
Regeneration systems are sized for the circulation rate required to remove the water vapor from the natural gas stream. Smaller regeneration skids can be paired with larger towers for applications where minimal water vapor removal is required or a larger regeneration skid may be required for applications where high water content removal is needed.