Attached are
1. The laser lock box settings via screenshot in multi-instrument mode using the PLL as the modulation setting.
2. Diagram of multi-instrument mode for reference.
3. Ariel photo of the set up.
4. Inkscape drawing of the set up.
Also should note when scanning the cavity using the current it should be safe to use the full range (2V). The TEC controller should be set to ~10.5kOhms, but double check the range on the integrator is roughly centered.
https://imgur.com/a/udiuJuG
The log isn't letting me upload the photo of the lab. Uploaded to imgur instead.
I was able to upload the file here
I had an impromptu meeting/tour with Maty Lesovsky. The following are the notes I took
Good needle valves for bringing things up to pressure
All metal angle valves
Avoid rubber oring
10^-10 l mbar/s cm^2 is LIGO’s desorption
Have metal bake out site
All metal bake out valves
KJL has rubber o ring which sucks in contaminants
Varian is a good brand
VAT makes large ones
Use research grade N2 if you want to backfil
Can hook up to needle valve
Clean air cheaper
They have an SRS RGA 200
Realistically only gets to 100 amu
Hanford uses 1000, but this SRS should be plenty
Have custom controllers for bake out
8 W/ft
Takes 110-220 V
PID controller from computer, can tell ramp time and other parameters
They have prints of the circuits
They have thermistors on the outside
Get surface temperature, not in air
Tac weld for surface temperature
Omega or McMaster
They also have insulation we can use
200°C is standard for small stainless
This is 150°C because it’s so large
They think they’ll keep the turbo on during the bake out
Biggest concern is machining oils
Fiberglass tape (from McMaster)
Goes up to 300°C
Great for holding thermocouples
Has gone through hundreds of bake outs over years, been fine
Avoid fiberglass insulation
Iwata Scroll Meister pumps, equivalent to the IDP-7
Tri scroll
Have mufflers to trap chemicals out of them
Smart to have a safety shutoff in case you lose power
Cut power to turbo
Choke turbo if it comes back on with pressure
Do a rate of rise test on partial volumes and the whole system
Good to test if something is degrading
Have a battery backup for a couple hours to run the turbo so the turbo breaks don’t wear out
For controllers, have Terranova Model 934 wide range which are good
MKS PDR 2000 also nice and easy
Invest in a case to display everything
They have a lab view program to monitor the pressure and the RGA
Using https://vacuum-calculator.pfeiffer-vacuum.com and the previous post's volume and surface area data, I have some inital impressions of our pump requirements for the 8 m long interferometer.
Other assumptions:
Desoprtion: 1e-9 mbar*l/(s*cm²)
Leak rate: 3e-9 mbar*l/s
1. Our final pressure limitation will be a function of desorption, not leak rate, because our surface area is so huge
2. The time to reach 6 Torr, where Pfeiffer starts the turbos, is given approximately by 1 hr * (4.3 m^3/h rougher pumping speed / pump roughing speed)
3.
A. 3 HiPace 80 DN 63 get to a pressure of 10^-7 Torr in 12 hours, 10^-8 Torr in a week
B. 1 HiPace 80 DN 63 gets to a pressure of 10^-7 Torr in 36 hours, 5*10^-8 Torr in a week
4. A 1 m, 6.45 mm tube between the roughers and the turbos doesn't greatly affect the pump down time or the final pressure
To get the round trip Gouy phase of the cavity to 1/3, the total round trip length should be 2.4 m.
Current mirror locations: (X,Y) = (10.655 in, 1.1033 in)
Current total round trip length = 4*X+4*sqrt(X2+Y2) = 85.47 in = 2.17 m
Need 2.4 m, so need to add 0.23 m = 9 in
This means every mirror needs to go 9 in / 8 = 1.125 in back
8 comes from 4 mirrors and the round trip
New mirror locations: (X,Y) = (11.779 in, 1.163 in)
New total round trip length = 4*X+4*sqrt(X2+Y2) = 94.46 in = 2.40 m
Thus, I plan on buying sixteen 1.125 in spacers for the every mirror.
Central vessel:
Treating as a cylinder
11.9 inch radius
11 inch height
V = pi*r^2*h = 4900 in^3 = 0.080 m^3
SA = 2*pi*r*h + 2*pi*r^2 = 1,700 in^2 = 1.1 m^2
End cube:
Treating as a cube, even though the inside is more spherical
L = 10 in
V = L^3 = 1,000 in^3 = 0.016 m^3
SA = 6*L^2 = 600 in^2 = 0.39 m^2
Tubes:
4 inch radius
275 in height (two 10 ft tubes + 1 ft T = 6.4 m, round up to 7 m including gate valve, reducer, etc)
V = pi*r^2*h = 13,800 in^3 = 0.23 m^3
SA = 2*pi*r*h = 6,900 in^2 = 4.5 m^2
Total:
Vessel + 5 Cubes + 2.1 Tubes (power recylcer ~0.7m):
V = 0.643 m^3 = 643 L
SA = 12.5 m^2
Assumed desorption: 1e-8 mbar*l/(s*cm²)
Assumed leak rate: 3e-9 mbar*l/s
Can then figure out what pumps and how many to use using the calculator