Converting oil-sealed pumps to dry pumps on older process tools
When a dry pump conversion pays off on an etcher, CVD tool or evaporator, how to size the replacement and what changes in facilities and interlocks.
We replace oil-sealed roughing pumps with dry pumps sized to your process, and adapt the foreline, purge and exhaust, to end oil changes and oil back-streaming.
Many older etch, PECVD, LPCVD, sputter and implant tools were built with oil-sealed rotary vane roughing pumps. On a clean process they are reliable. On a corrosive or deposition process they are a constant job: the oil degrades and must be changed often, filters and oil mist eliminators load up, and spent oil is hazardous waste because it carries process residue. Under some conditions oil vapour can also back-stream into the foreline and towards the chamber.
Corrosive processes often run these pumps on PFPE oil to resist attack, which adds to the consumable cost. A dry pump conversion replaces the oil-sealed pump with a pump that has no oil in the pumping path. For the longer reasoning and the pitfalls, see converting oil-sealed pumps to dry pumps.
The pump has to match the process, not only the tool. We look at:
Multi-stage roots and claw dry pumps are typical for corrosive and deposition duty. Scroll pumps suit clean, low-load uses such as load locks and some metrology tools. We state the type and the reasons in the proposal.
A typical conversion covers:
If the pumps are being replaced anyway during a vacuum system refurbishment, the conversion is done in the same stop.
Downtime is set mainly by facilities work at the pump location, such as a new purge line, cooling water or a power supply. If those are prepared in advance, the swap and verification on the tool are usually a short planned stop. The proposal states the planned downtime.
You receive the sizing note, before and after vacuum data, a facilities list and the service interval for the new pump. The upgrade applies widely to etch tools, deposition tools and implanters.
We review the gases, flows, pressures and duty cycle the pump has to handle.
We propose a dry pump type and size, with its purge, cooling and power needs.
Our engineers remove the oil pump, clean the foreline and fit the dry pump with purge and exhaust.
We compare pump-down time, base pressure and process pressure control with the baseline.
On corrosive or deposition processes oil pumps need frequent oil changes, the oil carries process residue into the waste stream, and oil can back-stream into the foreline. A dry pump removes those problems and usually lowers routine maintenance.
Often yes. Many dry pumps need N2 purge, cooling water and more electrical power than the oil pump they replace, so we confirm facilities before choosing the pump.
It depends on the process. Multi-stage roots and claw pumps are common on corrosive and deposition processes, and scroll pumps suit clean, low-load duty such as load locks.
Usually only partly. We clean out residual oil, replace flex lines and seals that are oil-soaked or damaged, and add a purge connection if the pump needs one.
When a dry pump conversion pays off on an etcher, CVD tool or evaporator, how to size the replacement and what changes in facilities and interlocks.
Tell us the tool and what you need. We scope the work and send a written offer.