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Current study status of high gradient at KEK Fumio Furuta KEK SCRF meeting Fermilab. Apr. 21-25 2008. Single cell cavity status (ICHIRO center cell shape). Ave. Eacc=46.7 ± 1.9 MV/m. ACD: Qo=0.8e10@40MV/m. ACD target. Recipe : CBP(100um)+CP(10um)+EP(80um) - PowerPoint PPT Presentation
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Current study status of high gradient at KEK
Fumio Furuta
KEK
SCRF meeting Fermilab. Apr. 21-25 2008
108
109
1010
1011
0 10 20 30 40 50 60
IS#2IS#3IS#4IS#5IS#7CLG#1
Qo
Eacc[MV/m]
0 10 20 30 40 50 60
Num
ber
Eacc [MV/m]
1
2
3
4
5
N=6
ACD targetACD: Qo=0.8e10@40MV/m
Ave. Eacc=46.7±1.9MV/m
Single cell cavity status (ICHIRO center cell shape)
Recipe : CBP(100um)+CP(10um)+EP(80um) +EP(20m)+flash EP(3m) +HPR+Baking
Narrow scattering, high performance.
MP process needed. How to eliminate MP?
Strengthen rinsing after EP.
ICHIRO 9-cell cavity status
108
109
1010
1011
0 10 20 30 40 50
Qo
Eacc [MV/m]
9cell #0 w/o HOMEacc=29.3Qo=1.02e10
quench
9cell #1 w/ HOMEacc=19.08MV/mQo=3.64e9
FE9cell-#1~#3
9cell-#0 (w/o HOM)
MP barrier at taper of BP
FE caused by end group
Large beam tube, complicated structure of end group
Contamination from HPR pump by long operation.
Key points
Re-design of ICHIRO and end-single cell study
Replacement of HPR pump: plunger->diaphragm
108
109
1010
1011
0 10 20 30 40 50 60
Qo
Eacc [MV/m]
2007/3/7 Wed.
Eacc=6.92MV/mQo=6.76e9 @2K
limited by FE
X-ray >6MV/m.
HPR(UPW@Nomura, 3/6)TOC=5ppb, Bacteria=
Field Emission by Plunger HPR Pump contamination
Final filter -before use- Contaminated
Silicon greaseused at plunger sealing of HPR pump!
HPR pump was replaced to diaphragm type on beginning of Sep. 2007
Successfully Qualified by single cell cavity tests!
Fixed!
108
109
1010
1011
0 10 20 30 40 50 60
Qo
Eacc [MV/m]108
109
1010
1011
0 10 20 30 40 50 60
Qo
Eacc [MV/m]
108
109
1010
1011
0 10 20 30 40 50 60
Qo
Eacc [MV/m]
108
109
1010
1011
0 10 20 30 40 50 60
Qo
Eacc [MV/m]
42MV/m
45MV/m
ISE#2 (old)
ISE#3 (new)
ISE#4 (new)
ISE#5 (old end group)
Full HOM
Just HOM cylinder
50MV/m
52MV/m
Ethanol Rinsing
Ethanol Rinsing
End-single cell cavities
End-cell shape has no problem.
Ethanol rinse has big effects on end groups.
ISE#5 tight loop test
EP(20m)+flash EP(3m) +Ethanol rinsing (10min., r.t.) +Degreasing(MICRO-90, 2%, 1hr, 50C) +HPR(Nomura, UPW) +Baking(120C*48hrs)
Eacc[MV/m] Qo
3rd 40.2 9.43e9
4th 39.9 8.83e9
5th 31.1 4.98e9
12th 45.1 8.63e9
Repeat
ISE#5
Full HOM
108
109
1010
1011
0 10 20 30 40 50
3rd4th5th12th
Qo
Eacc [MV/m]
9-cell = + x7 + = 50MV/m?
Center-cellend-cell end-cell
Old
New
Redesigned 9-cell cavity : New Ichiro 9-cell
Ready to EP, VT
I9#5→sent to J-lab (EP+VT)*3.
108
109
1010
1011
0 10 20 30 40 50
ICHIRO5_17feb08_test4(CW)
CW meas.pulse meas.
Qo
Eacc [MV/m]
Eacc=36.5MV/mQo=5.94e9 @2K
limited by FE
X-ray>20MV/m,(>1mRad/hr)
#5, #6 :w/o end groups
#7, #8 :w/ end groups
+EP(20m) + Degreasing + HPR
+EP(20m) + flash EP(3m) + Degreasing + Ethanol rinsing + HPR
+EP(20m) + Ethanol rinsing + HPR
will be tested
Studies for strengthen rinsing by single cell cavities
+EP(20m) + flash EP(3m) + HPR
High reliability, but still MP process needed.
Well work for reduction of MP.
Well work for end group rinsing.
Need more statistics.
(A)
(B)
(C)
(D)
46.7±1.9MV/m (N=6)
44.2±6.4MV/m (N=5)
Summary
・ Surface treatment recipe for single cell (center cell shape) was almost fixed. Degreasing has effect on reduction of MP.
・ Limitations of ICHIRO 9-cell (#0,1,2 and 3) cavities were related to end group and contamination from plunger HPR pump.
・ Plunger pump was replaced to diaphragm pump, it works well.
・ End-cell shape single cell cavities were fabricated and tested to understand the end groups.
・ Ethanol rinsing have effect on end group rinsing. End cell cavity with full end group reached 45MV/m. For the end single cell cavities, more statistics will be collected.
・ 4 re-designed ICHIRO 9-cell (#5, 6, 7, and 8) were fabricated.
#5 and #6 have simple beam tube, #5 was tested and reached 36MV/m at J-lab.
#7 and #8 have full end group, will be tested next month at KEK.