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LC Isolink Liquid Chromatography Operation LC Startup Overview
Note: When operating: Total combined flow of MS pump, oxidation pump, and acid pump cannot exceed 700
µl/min. Over-pressuring the line can damage the Isolink separation unit. Isolink Operational Settings
************************************************************************ LC Shutdown Overview
************************************************************************ Maximum Flow Rate (Pumps)
************************************************************************ Detailed LC
Instructions
i. Slight
Vacuum: Apply a slight vacuum.
ii. Ultrasonic
Bath: Treat the reagents in an ultrasonic bath at this slight vacuum and
30 ¼C-40 ¼C. CO2 dissolved in the liquid will thus be volatilized. As both
oxidation reagent and acid/catalyst mixture are acidic media, nearly no CO2 will be
re-dissolved.
iii. Helium
Stripping: As a protective measure, perform a slight helium stripping using
e.g. a capillary that is directly introduced and continuously fed with helium.
The helium atmosphere prevents re-gassing, and dissolved CO2 will thus be
stripped out of the liquid. The same procedure is valid for the water at the
HPLC pump, which even is already equipped with a degasser: in addition to this
degasser, it is necessary to degas the water before use (first via slight
vacuum followed by ultrasonic bath and concluded by helium stripping). Leave the water under a
helium atmosphere by providing a constant helium stream.
i. Backpiston Flushing of HPLC Pump
ii. Bacteria Note: If the CO2 background signal
nevertheless is still considerably high after purging with water, eliminate remaining
bacteria by oxidation: therefore, purge the HPLC unit including the HPLC pulse
damper with oxidation reagent daily before measurement. A lower concentration
of M2S2O8 (M+ = Na+, K+, NH4+) than that used for
measurements is sufficient, e.g. 50-100 g/l. Finally purge several times using
pure water.
i. Fill the solvent
bottle(s) with degassed water and/or water inorganic solvent mix.
ii. Insert the tip of a 10
mL syringe into the tubing that is connected to the wingnut of the LDA (liquid
displacement assembly).
iii. Open the wingnut by
turning it counter-clockwise.
iv. Turn-on the pump power.
v. Open direct control
software in Isodat. 1.
Enter
percentages of solvent lines (100% Line A if just water). 2.
Enter
flow rate to 2000 µL/min. 3.
Click
Start Run (blue triangle) to start pump flow. You
may need to stop the pump to empty the syringe periodically. 4.
After
purging is complete, stop the pump and close the wingnut.
i. Fill the solvent
reservoir with degassed water, or weak inorganic oxidizing solution.
ii. Make sure a flow
restrictor or HPLC column is attached to the pulse dampener outlet
iii. Insert the tip of a 10
ml syringe to the manual bleed valve of the pulse dampener, and then open the
wingnut by turning it counter-clockwise.
iv. Set the pump flow to
1000 µl/min.
v. Fill the loop completely
to expel any air bubbles that may be in the line, or continue flushing to free
the lines of bacteria followed by a degassed water (solvent) flush.
vi. Set the pumprate to the
appropriate for the application.
vii. After the Pulse Dampener
has been refilled with degassed wager, close the manual feeder valve (wingnut
clockwise).
i. Cut the 1/8Ó OD x 1/16Ó
ID PTFE tubing of the outer loop of the piston.
ii. Connect a syringe filled
with degassed HPLC grade water to the bottom piece of the tubing and gently
flush water through the system.
iii. Reattach a new piece of
tubing (DO I NEED TO FINISH BY PUSHING AIR THROUGH THE SYSTEM WHEN DONE
FLUSHING????).
i. Rinse the
containers using LC-grade solvent to remove any dust.
ii. Fill the
containers with appropriate LC-grade solvent.
iii. The bottle
caps are pre-assembled to include an inlet line and filter. Ensure that each
filter is tightly assembled to its fitting, and that the filter fitting is
firmly attached to the inlet line. Mace the solvent filter inlet line into each
bottle, making sure that the inlet filter rests on the bottom of the bottle.
Cap the bottle.
iv. Attach the
appropriate label to each solvent bottle cap to identify it.
v. Run vent
lines from each bottle to an appropriate exhaust apparatus.
i. oxidation
reagent 1.
200 g/l M2S2O8 (M+ = Na+, K+, NH4+);
this will yield a strongly oxidative solution. 2.
For UCSC test: 40 gm Na2S2O8 was
dissolved in 200 ml H2O. However, what ultimately worked best was
dissolving 15 g Na2S2O8 in 500 ml H2O. 3.
If no AgNO3 catalyst is used, increase the
concentration to 50 gm Na2S2O8 in 200 ml H2O.
4.
Measure water using a graduated cylinder.
ii. acid 1.
1.5 molar solution of H3PO4 in water
iii. catalyst 1.
Catalytic amounts of solid AgNO3 are used, e.g. three tips of
spatula in 200 ml water. Compared to an aqueous solution of AgNO3, solid AgNO3 is
advantageous, as: a.
no impurities due to
additional water will enter the system and b.
no additional water needs to be degassed.
iv. The acid/catalyst
mixture is composed of: 1.
aqueous
85% ortho-phosphoric acid, H3PO4 2.
silver
nitrate, AgNO3. Silver ions (Ag+) are catalytically
active as they temporarily fix oxygen and transfer it to the organic compounds.
These, in turn, will be oxidized to CO2. 3.
Warning. In case of
sulfide- or halogenide-containing samples, e.g. chloride in seawater, do not
use silver nitrate, AgNO3, as an oxidative catalyst! As precipitates, sparingly soluble
silver sulfide, Ag2S or silver halogenides, AgX would be formed causing damage to the
separation unit. 4.
These
are the recommended acid/catalyst concentrations given by Dieter (of Thermo-Bremen), as relayed to UCSC
by installation engineer Burt Wolff.
v. Note. It is unreasonable to
recommend any generally accepted concentration values. Rather, the optimum
concentrations of all reagent components must always be determined empirically.
vi. Principle: On the one hand, oxidation
reagent concentration must be sufficiently high to ensure complete oxidation
(check via oxygen background; see Oxygen Background (m/z 32) on page 7-6).
vii. If its concentration is too
high, however, the solutions show increased viscosity. Therefore, they are more
difficult to be pumped, and lifetime of the system might be reduced due to
corrosion.
i. double peaks (a small
peak is followed by a big one)
ii. peak broadening
iii. extraordinary long
tailing (additionally, δ 13C
values may diverge).
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