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2019/05/20 (Monday)

Previous Day

Status: Transferred LN2 yesterday
0931 MC(Cernox) = 4.68 K, Sorb/1K Pot = 8.6/6.8 K, G1 (fridge) = 561 mbar, MB = 38.6%
0938 Fill LN2 cold trap full.
0940 IVC = 0.86 nbar, 4.6 nbar with pump valved out.
0956 Perform 4K electrical check, all good including DIB4 PD SQUID
1015 We want to look at the shorted channel (ZC-13 PB/DIB3 PB) as we cool down to try and understand the SQUID temperature. Hopefully we can make the SQUID work at these temps.
1020 Start up MIDAS. Let's set up DCRC3 to look at DIB3.
1045 Power up DCRC3 and start MIDAS programs. With whatever SQUID settings were left on DCRC3 and QET bias=0, we can see some noise signal on channels PB, PC, PD. PA is railed.
1155 SQUIDs seem to be working. Adjust DCRC3 PB SQUID settings to SQUID bias/lockpoint = -80/-4 to achieve nice modulation curve.
1202 Try to tune DCRC3 PD SQUID as well so we can look at SQUID only noise, but it looks stanky. Ah, we ought to Zap SQUIDs.
1203 Zap DIB 3 SQUIDs
1215 Tune DIB3 PD SQUID to SQUID bias/lockpoint = -80/-4 to achieve nice modulation curve.
1220 Just looking at PSDs on the pulse viewer, it looks like DIB3 PD (SQUID only) has very low, flat noise at around 3e-7 (in some units? Not sure how the SQUID tuning GUI PSD is normalized). DIB3 PB has a flat spectrum at 4.2e-6 with R/L roll off as expected for Johnson noise.
1222 Increase trace length to 52.4288 ms. PSDs look nice.
1227 MC(Cernox) = 4.75 K, Sorb/1K Pot = 8.7/6.9 K, G1 (fridge) = 557 mbar
1230 Let's try a baby IbIs with DCRC3 pB. Looks nice and linear with slope of -16.5 mV/uA
As described on the Run 70 summary, this implies a wirebond resistance of 5.5 mΩ
Ib (uA) Vo (V)
-10 0.917
-5 0.8349
0 0.7529
5 0.6705
10 0.5868
1232 Let's also record some data for further noise analysis.
1234 Start 100s series with 20 Hz in run randoms and 1000 BOR randoms, DCRC3 PB/PD QET bias = 0
1235 Okay, so we'll need to do a LHe transfer soon. After that, we'll start the 1K pot and cool down further. While that's happening, we'll periodically take baby IbIs and randoms data as above to try and track resistances and temperatures at the SQUID card.
1315 Commence LHe transfer. MB = 34.0%
1400 Commence LHe transfer. MB = 88.6%
1405 MC(Cernox) = 4.75 K, Sorb/1K Pot = 6.3/5.0 K, Turbo on IVC = 0.54 nbar, G1 (fridge) = 518 mbar
1406 Pump out 1K pot line up to speedivalve with scroll pump.
1415 Switch over to 4he pump. Change pump exhaust to recovery.
1418 Check pressure in 1K Pot: about 0.17 bar on the mechanical gauge.
1425 Pump out 1K Pot in steps, alternating between V4a and the 1K Pot speedivalve. After 4 iterations get pot down to < 0.1 bar. Then leave 4He pump pumping on pot continuously.
1427 1K Pot = 4.5 K / 0.28 mbar, MC = 4.75 K
1430 Open 1K Pot needle valve → 10°. 1K Pot → 4.1 K / 0.45 mbar
1435 Open 1K Pot needle valve → 20°. 1K Pot → 4.1 K / 0.45 mbar
Open 1K Pot needle valve → 30°. 1K Pot → 4.1 K / 0.50 mbar
Why isn't it cooling?
1440 Maybe the needle valve is crudded up? Close it and open back to 30°. 1K Pot → 4.1 K / 0.50 mbar
1444 Open 1K Pot needle valve → 40°. 1K Pot → 4.2 K / 0.55 mbar
1445 Open 1K Pot needle valve → 50°. No change.
Open 1K Pot needle valve → 60°. No change.
Open 1K Pot needle valve → 70°. No change.
Open 1K Pot needle valve → 80°. No change.
1448 Close 1K Pot needle valve then open it back up to 90°. 1K Pot → 4.2 K / 0.60 mbar
1454 Slowly 1K open needle valve until it's 2 full rotation open. No change: 1K Pot → 4.2 K / 0.60 mbar
Close 1K Pot needle valve completely.
1459 This feels like the 1K Pot siphon line is plugged like on 2018\05\16.
1502 With needle valve closed, close valve at 4He pump and watch P2. It runs off to P2>1000 mbar within a few seconds.
1530 Played with needle valve a bunch, nothing really seemed to matter.
1545 With needle valve closed, P2 starts rising to hundreds of mbar. What's going on??
Close 1K Pot speedivalve and P2 starts to fall, but doesn't get below 10s of mbar. Close V4, P2 sits at 10 mbar.
1548 Try switching pump exhaust from recovery to air. There is a huge whoosh as a bunch of pressure comes out and P2 falls to < 1mbar as it should.
Ahhh! We realize that we had opened the 4He pump exhaust to recovery with the yellow valve, but had not opened the red valve connecting the 1K pot exhaust line to recovery!
1556 Open 1K Pot to recovery with the yellow valve and by opening the red wall valve.
1558 Do the same 1K pot steps as above: Check pressure in 1K Pot on the mechanical gauge, pump out 1K Pot in steps, alternating between V4a and the 1K Pot speedivalve, until pot is down to < 0.1 bar, then leave 4He pump pumping on pot continuously.
1600 1K pot = 4.2 K / 0.50 mbar
1601 Open 1K Pot needle valve → 10°. 1K Pot → 4.2 K / 0.55 mbar
Open 1K Pot needle valve → 20°. 1K Pot → 4.2 K / 0.55 mbar
1605 Slowly open 1K Pot needle valve. At 60°, P2 rises to 1.7 mbar, but no change in temperature.
Open to 80°, no change.
1615 Again, play with needle valve a bit, opening it as far as 4 full rotations, but P2 never rises above 1.7 mbar and 1K Pot temp never moves far from 4.2 K
Now I'm sure the 1K Pot is clogged. We'll have to warm up to 300 K and try again. [image not archived: sad.svg]
1620 Close 1K Pot needle valve and speedivalve. Close off valve to 4He pump and turn off pump. Close recovery valve
1622 Stop pumping IVC with turbo. IVC pressure = 3.0 nbar
1627 Let 2 hose-lengths He into IVC. IVC → 86 ubar. MC and 1K Pot temperatures fall to ~4.3 K
1635 MB = 87.8%. Recovery rate = 300 sec/cubicft
1640 Start pumping mix to dump.
1650 Let 1.9 mbar He gas into vacuum manifold. Then open cryostat vacuum jacket valve to let this into the vacuum jacket. Vacuum jacket → 34 μbar, Recovery rate → 34 sec/cubicft
This isn't a very aggressive rate, but it should be fine for overnight.
1710 Set up webcam connected to jiajin to watch LHe level meter overnight. We'll take a pic every 5 min and sort through them in the morning. It's also updating the website so we can check the level overnight.
1835 MB = 78.3%
2135 MB = 70.7%

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