9048 J. Phys. Chem. A, Vol. 111, No. 37, 2007
Butkovskaya et al.
-
HNO3 was detected using the reaction with SF6 , giving the
4
peak at m/e 82:
SF6- + HNO f NO ‚(HF) + SF
-
(4i)
3
3
5
The branching ratio of reaction 1, â ) k1b/k1a, was obtained by
measuring the concentration ratio of the HNO3 and NO2
products from channels 1b and 1a, respectively. To convert the
measured intensity ratio of the products, ∆I82/∆I46, to the
concentration ratio, it is necessary to know the ratio of the
apparatus sensitivities to HNO3 and NO2, SHNO3/SNO2. The SHNO3/
SNO2 ratio and the absolute sensitivities themselves are deter-
mined by a number of parameters which vary with changing
the pressure in the TFR. The most important parameters include
pressure and flow velocity in the IMR, sampling conditions at
the interface between the TFR and IMR, optimum potentials
applied to the sampling cone, and the ion optics elements behind
it. To account for the dependence of the sensitivities on the
pressure in the TFR, the following approach was adopted. At
P ) 200 Torr, the absolute and relative sensitivities were
determined using a calibration method described in our previous
Figure 1. Experimental setup: 1, ion source; 2, ion-molecule reactor;
3
7
, temperature controller; 4, ,turbulizer.; 5, injector; 6, resistance;
, cooling bath; 8, discharge tube; 9, microwave discharge; 10, sampling
II
cones; 11, temperature sensor; 12, Fe (SO
4
) filter; 13, cool bath; 14,
NO cylinder.
HO2 radicals were produced in the TFR by the reaction
H + O + M f HO + M
(3)
2
2
1
study. In brief, the three-step procedure consisted of (1) NO2
calibration using a standard NO2 gas mixture, (2) OH calibration
using reaction 5 at short reaction times and low NO2 concentra-
tions, and (3) calibration of nitric acid by measuring the kinetics
of the OH decay and appearance of HNO3 in reaction 4:
with H-atoms generated by a microwave discharge in H2/He
gas mixtures flowing through a quartz tube concentrically
connected to the movable injector. The flows of N2 in the
injector and of He in the discharge tube were optimized
for maximum H-atoms production. He (AlphaGaz 2) was
purified by passing through molecular sieves cooled by
liquid N2. Tank grade H2 (AlphaGaz 2) was used without
further purification. NO was introduced into the TFR upstream
of the tip of the injector. The tank grade NO (AlphaGaz N20)
passed successively through ethanol/liquid nitrogen cooled
H + NO f OH + NO
(5)
(4)
2
OH + NO + M f HNO + M
2
3
The advantages of such “chemical” calibration are (i) in situ
production of HNO3 that eliminates the problems connected with
the introduction of HNO3 into the reactor and (ii) absence of
the errors connected with the determination of NO2 concentra-
tion, as these errors vanish in the sensitivity ratio SHNO3/SNO2.
This procedure was also used in some experiments at P ) 100,
II
traps and Fe (SO4) filter to remove NO2 and heavier nitrogen
oxides. NO flow rate of about 0.6 SCCM was maintained
using a TYLAN flow controller. O2 (AlphaGaz 2) and CO
(
AlphaGaz N47) were added into the main N2 stream using
CELERITY flow controllers. The maximum distance from the
injector tip to the orifice of the inlet cone of the ion-molecule
reactor was L ) 50 cm, which corresponded to a reaction
time in the TFR of about t ) 30 ms at P ) 200 Torr and T )
3
00, 400, and 500 Torr. However, to avoid potential problems
related to increasing formation of peroxynitrous acid, HOONO,
5
with pressure in reaction 4 and to simplify the calibration
2
98 K.
.2. CIMS Detection and Sensitivity. Gas mixtures from
procedure for other pressures in the TFR, the SHNO3/SNO2 ratios
were derived from the changes of NO2 and HNO3 sensitivities
relative to those at 200 Torr determined from direct introduction
of HNO3 and NO2 into the TFR.
2
the TFR were sampled through a Teflon cone with orifice
diameter of 0.5 mm into the ion-molecule reactor (IMR) located
perpendicular to the TFR. The flow rate of the Ar carrier gas
in the IMR was 3.6 SLPM at the typical pressure of 0.7 Torr.
The change of SHNO3 with pressure was determined by flowing
gaseous HNO3 from the mixture of HNO3 (Aldrich, 69%) and
H2SO4 (Sigma-Aldrich, 90%) aqueous solutions (10:1 volume
ratio) into the reactor. Gaseous HNO3 was transported by a He
flow bubbling through the solution mixture in a glass trap. The
trap was kept below 16 °C to avoid saturation of the HNO3
signal. The helium flow was varied by means of a CELERITY
mass flow controller with 10 SCCM maximum flow rate. A
dilution by larger He flow regulated using a 250 SCCM TYLAN
flow controller took place shortly downstream of the trap. The
trap was connected to the reactor via a PFA tube. At each
pressure SHNO3 was determined from the linear increase of the
signal intensity at m/e 82 with the flow rate of He passing
through the bubbler. The HNO3 partial pressure over the
solution, PHNO3, was not known, but this was not critical because
only the sensitivities relative to those at 200 Torr, SP/S200 (HNO3)
+
The primary Ar ions and electrons were generated in the ion
source by a heated filament. The emission current from the
filament was always stabilized during the measurements. SF6
was continuously introduced into the IMR downstream of the
ion source. The primary SF6- negative ions were produced by
attachment of thermalized electrons to SF6.
-
OH radicals and NO2 were detected as OH (m/e 17) and
-
- 2
NO2 (m/e 46) ions formed by electron transfer from SF6 :
SF6- + OH f OH + SF6
-
(1i)
(2i)
SF6- + NO f NO2 + SF6
-
2
HO2 radicals were detected at m/e 140 using the reaction3
SF6- + HO f [SF ‚O ] + other products
)
SHNO3(P)/SHNO3(200), were used. A rough estimation using
the average ratio SHNO3/SNO2 ≈ 4 from the chemical calibration
-
(3i)
2
4
2
at 200 Torr gave PHNO3 ≈ 0.03 Torr at 15 °C.