Goutelle 2011
Goutelle 2011
Hydroxyethylhydrazine by
the Raschig Process and
Comparison with Synthesis
by the Alkylation Process
V. GOUTELLE, V. PASQUET, A. EL HAJJ, A. J. BOUGRINE, H. DELALU
Laboratoire Hydrazines et Procédés, Université Claude Bernard Lyon 1, UMR CNRS 5179, Bâtiment Berthollet, 22 Avenue
Gaston Berger, F-69622 Villeurbanne Cedex, France
Received 18 May 2010; revised 16 November 2010, 22 February 2011; accepted 26 February 2011
DOI 10.1002/kin.20559
Published online 27 April 2011 in Wiley Online Library (wileyonlinelibrary.com).
ABSTRACT: The Raschig synthesis of hydroxyethylhydrazine (HEH) is studied, that is, the reac-
tion of monochloramine on ethanolamine. The formation of HEH is monitored by UV spectrom-
etry, and the influence of temperature and pH is studied. The primary reaction is an SN2 -type
mechanism, whereas the main secondary reaction is the oxidation of HEH by monochloramine.
This reaction is also monitored by UV spectrometry, and the oxidation product is identified by
GC–MS analysis, showing the formation of hydroxyethylhydrazone. The reaction mechanisms
and the rate constants were determined, and the results permit establishing the main reactions
occurring during HEH synthesis. These reactions were validated in a concentrated medium,
with the systematic study of the influence of the molar ratio p ([HEH]0 /[NH2 Cl]0 ) and the
final sodium hydroxide concentration and temperature. A comparison is made with the other
synthesis process already published, that is, the alkylation of hydrazine by either chloroethanol
or epoxide. C 2011 Wiley Periodicals, Inc. Int J Chem Kinet 43: 331–344, 2011
Since that time, the interest in this molecule has The Apparatus and Experimental Protocol
remained relevant.
The apparatus was composed of two parts: The upper
In a previous paper [4], HEH was synthesized by
part consisted of a double-walled cylindrical bulb with
alkylation of N2 H4 with 2-chloroethanol (CletOH)
a capacity of 200 mL in which a temperature sensor was
with or without a strong base. Another widely used
introduced. A wide diameter needle valve at the base of
method is the Raschig process. However, it has two
the bulb ensured that the liquid flowed rapidly. The bulb
main disadvantages: low reagent concentrations, espe-
was connected to the lower part which was a thermo-
cially chloramine, and a large number of secondary
static reactor with a capacity of 500 mL. Several inlets
reactions. On the other hand, it has several advantages:
allowed the introduction of nitrogen into the reactor,
the reaction is carried out in water, the reagents are
taking samples and measuring temperature. Agitation
less pollutant and expensive, and the process does not
was ensured by using a magnetic stirring bar. The bulb
use highly toxic reagents such as carcinogenic nitrate
and the reactor were kept at constant temperature by
and nitroso derivatives, thereby preserving the envi-
using a Julabo cryo-thermostat.
ronment. Thus, the aim of this paper is to describe
The ethanolamine (EA) or HEH solution (50 mL)
HEH synthesis by using the Raschig process and its
was introduced under nitrogen into the reactor, whereas
advantages and then compare the two methods.
the NH2 Cl solution (50 mL) was introduced into the
upper part. When the temperature was homogeneous,
the reagents were mixed together and samples were
taken under nitrogen.
EXPERIMENTAL
Reagents Analyses
Ethanolamine (99% purity) was provided by Aldrich, The different reactions involved in the system
and ammonia in aqueous solution (32%) was provided EA/NH2 Cl were studied by ultraviolet (UV) either
by Prolabo. The solutions of sodium hypochlorite at directly or by HPLC (high performance liquid chro-
48◦ chlorometry were provided by ELF-ATOCHEM, matography). The reaction products were character-
kept at 5◦ C, and systematically analyzed before use. ized by coupled GC–MS (gas chromatography–mass
Monochloramine (NH2 Cl) is not commercially spectrometry).
available so it was prepared at −10◦ C by reacting The different tests were carried out at pH 12.89 and
sodium hypochlorite (25 mL, 48◦ chlorometry) with T = 25◦ C, in a reductive medium for HEH concentra-
a mixed ammonia solution NH3 /NH4 Cl (25 mL, 3.6 tions between 8 and 40 × 10−3 M.
M/2.38 M) in the presence of ethyl ether (40 mL). For
the kinetic studies, NH2 Cl was purified by successive UV Spectrometry. A CARY 100 dual beam spectrom-
extractions with water and then stored at 5◦ C in ethyl eter from VARIAN was used (quartz cells from 1 to
ether to keep it stable. The aqueous solutions were ob- 10 mm light pathway), linked to a data acquisition sys-
tained just before use by reextraction from the ether tem. This device can perform repetitive spectrum scans
phase. The residual solvent and ammonia traces were between 900 and 180 nm, programmable as a function
eliminated by vacuum treatment. At this stage of prepa- of time, measure absorbance at each wavelength, and
ration, the NH2 Cl concentration was between 0.1 and superpose and add curves.
0.15 M.
The other reagents and salts used in this study HPLC Analysis. Five milliliters of the synthesis so-
(NaOH, NH4 Cl, Na2 HPO4 , KH2 PO4 , etc.) were prod- lution was taken and added to the same volume of
ucts for analysis at +99% (reagents from Prolabo RP, ethyl ether. After mixing, the solution separated itself
Merck, Aldrich, etc.). into two phases and the upper phase was extracted and
Water was purified by using an ion exchange resin. conditioned at a temperature of 0◦ C. The two reagents
were isolated in each phase after which the sample was Absorbance (D)
analyzed. An Agilent 1100 chromatograph with a bar
1.4
iodine detector was used with an Eclipse ODS XDB-
C8 column (grafted phase octadecylsilane) of 150 mm
length and 3 mm diameter (dp = 5 μm). A precolumn 1.2
was used for basic injections. The mobile phase was
a mixture of 95% water/5% acetonitrile. The volume λ=λmax=243nm
of the manual injection loop was 20 μL, and the flow 1
rate was 0.5 mL/min. The wavelengths measured by
the bar iodine detector were established at λ = 200,
0.8
243, 254 nm.
Table I Determination of the Kinetic Parameters of the Reaction between NH2 Cl and EA (T = 25◦ C, [NaOH] = 0.1 M)
T (◦ C) [EA]0 (10−2 M) [NH2 Cl]0 (10−3 M) p = [EA]0 /[NH2 Cl]0 k1 (10−1 M−1 min−1 ) R2
25 2.2 2.8 7.9 1.62 0.999
25 2.6 2.8 9.2 1.61 0.998
25 3.2 2.9 11.2 1.62 0.999
25 4.8 2.9 16.2 1.62 0.998
25 6.1 2.9 21.4 1.61 0.993
precise determination of the rate laws from the NH2 Cl leads to the following equation:
concentration–time curves, limiting the measurement
to the half time of the reaction.
1 [NH2 Cl]0 [EA]
ln = k1 t (3)
[EA]0 − [NH2 Cl]0 [EA]0 [NH2 Cl]
The Rate Laws. The rate of NH2 Cl disappearance is
expressed by the relation (1) according to the two reac-
tions described above: formation of HEH from NH2 Cl The plot ln A/([EA]0 − [NH2 Cl]0 ) = f (t), with A =
and hydrolysis of NH2 Cl. [NH2 Cl]0 [EA]/[EA]0 [NH2 Cl] at 25◦ C, pH 12.89, and
a molar ratio p = [EA]/[NH2 Cl] = 11.2, is linear.
d[NH2 Cl] The straight line obtained goes through the origin with
− = ν1 k1 [NH2 Cl]α [EA]β a slope equal to 1.62 × 10−1 L mol−1 min−1 and a
dt
correlation coefficient R 2 = 0.999.
+ k2 [NH2 Cl] [OH− ] (1) A similar treatment was carried out for a series of
mixtures of different reagent compositions, to verify
where ν1 is the stoichiometry coefficient and k1 , α, invariability k1 at a fixed pH and temperature. The
β, respectively, the rate constant of the reaction com- uncertainty of measurement is about 5% for k1 and
pared to NH2 Cl and the partial orders compared to the the other kinetic parameters determined in this paper.
reagents. The second term is related to NH2 Cl hydrol- The results are presented in Table I.
ysis, which can be neglected under the experimental The values obtained are almost constant considering
conditions studied (pH < 13). the experimental errors. Thus, at T = 25◦ C and pH
The kinetic parameters were determined by integra- 12.89, the average value of k1 is 1.62 × 10−1 L mol−1
tion, by considering α = β = 1. Under these condi- min−1 .
tions, the NH2 Cl concentration was determined from
the absorbance at λ = 243 nm at each instant.
Influence of pH. Concerning the Raschig process, an
Dλ (t) increase in medium alkalinity generally leads to an
[NH2 Cl] =
εl increase in the reaction rate. A systematic study was
(ε = 4581 mol−1 cm−1 ; l = 1 cm) (2) carried out for HEH for a concentration of NaOH be-
tween 0.1 and 1 M. The pH values were calculated
by using the works of Akerlof and Kegeles [5,6] con-
For unity stoichiometry (ν = 1), the instantaneous con- cerning the determination of activity coefficients in
centration of EA was deduced by the formula concentrated solutions. The tests were carried out for
a constant concentration of NH2 Cl (∼2.9 × 10−3 M)
[EA] = [EA]0 − [NH2 Cl] and EA (∼60 × 10−3 M).
The application of the same analytical method leads
to an almost twofold increase in k1 (2.38 × 10−1 M−1
where [EA]0 represents the amine concentration at
min−1 at pH 14). However, these values require a cor-
t = 0.
rection because NH2 Cl hydrolysis cannot be neglected
By representing the initial NH2 Cl concentration by
under the experimental conditions studied. This reac-
[NH2 Cl]0 , the integration of relation (1),
tion was studied by Anbar and Yagil [7]. It follows
a kinetic law of order 2 compared to the reagents
[NH2 Cl]
d[NH2 Cl] t
(k2 = 62 × 10−6 M−1 s−1 or 3.72 × 10−3 M−1 min−1 at
− = k1 dt
[NH2 Cl]0 [NH2 Cl]([EA]0 − [NH2 Cl]) 0 T = 25◦ C).
Table II Influence of pH on the Hydrazine Formation Constant k1 and Its Corrected Value ϕ0 (T = 25◦ C)
pH [EA]0 (10−2 M) [NH2 Cl]0 (10−3 M) p = [EA]0 /[NH2 Cl]0 k1 (10−1 M−1 min−1 ) ϕ0 (10−1 M−1 min−1 )
12.9 6.1 2.9 21.4 1.61 1.55
13.2 6.0 2.9 21.0 1.71 1.59
13.6 6.1 2.9 21.5 2.04 1.65
13.8 6.0 2.8 21.4 2.38 1.76
Under these conditions, we can write The plot ln k1 = f(1/T) gives a straight line with a
slope –Ea /R and a y-intercept ln A1 . This corresponds
d[NH2 Cl] to the activation energy and to the Arrhenius factor:
− = [NH2 Cl](k1 [EA]0 + k2 [OH− ]0 )
dt
= ϕ0 [NH2 Cl] k1 = 3.06 × 107 exp(−57.5/RT)
(k −1 in M−1 s−1 , Ea1 in kJ mol−1 )
To ensure sufficient excess EA and during the first
moments of the reaction (isolation method), the term from which the enthalpy and the entropy can be de-
between brackets can be considered as constant. duced:
The bimolecular constant k1 can be written as
H10# = Ea1 − RT ; S10# = R ln(A1 h/ekB T ) (5)
ϕ0 − k2 [OH − ]0
k1 = (4)
[EA] 0 where kB and h represent the Boltzmann constant
and the Planck universal constant, respectively (kB =
The results for both treatments are reported in Table II.
1.380 × 10−23 J K−1 ; h = 6.623 × 10−34 J s).
After correction, we noted a moderate increase in the
This gives H10# = 55.0 kJ mol−1 and S10# =
reaction rate. Therefore, it is not useful to carry out the
−110 J K −1 mol−1 . The uncertainty of measurement
synthesis in a very alkaline medium.
is about 6% for these thermodynamic values.
Influence of Temperature. The influence of tempera- Mechanistic Aspect. The HEH formation mechanism
ture was studied between 15 and 45◦ C for NH2 Cl and is of the SN2 -type. The limiting step corresponds to
EA concentrations equal to 2.8 × 10−3 and 60 × 10−3 a nucleophilic attack of the electron doublet of the
M, respectively. The variation of k1 versus temperature nitrogen from the amine on the weakly electropositive
obeys Arrhenius’ law (Fig. 2). site of the nitrogen of the chlorinated derivative. Proton
elimination is instantaneous.
-1
1/T /K
-4 +
+ _
0.0031 0.0032 0.0033 0.0034 0.0035
HO-(CH2)2-NH2 + NH2-Cl [H2N-NH2-(CH2)2-OH] Cl
Table III Influence of Amine Nucleophilicity on the Hydrazine Formation Constant kf (pH 13 and T = 25◦ C)
Amine Substitution Degree Hydrazine Formed kf (M−1 s−1 ) T (◦ C) Reference
NH3 0 N2 H4 0.09 × 10−3 27.5 [12]
CH3 NH2 1 CH3 NHNH2 5.09 × 10−3 25 [13]
HO(CH2 )2 NH2 1 HO(CH2 )2 NHNH2 2.7 × 10−3 25
(CH3 )2 NH 2 (CH3 )2 NNH2 72 × 10−3 25 [14]
C7 H12 NH 2 (cyclic) C7 H12 NNH2 45.5 × 10−3 25 [15]
C5 H10 NH 2 (cyclic) C5 H10 NNH2 56 × 10−3 25 [16]
(CH3 )3 N 3 (CH3 )3 NNH2 205 × 10−3 27.5 [12]
(monomethylhydrazine CH3 NHNH2 ). This result is The UV analysis (Fig. 3) shows two consecutive
due to the electroattractive effect of the terminal hy- reaction processes: First, the decrease in the NH2 Cl
droxyl. peak at λ = 243 nm is limited by the increase of a
At pH ≤ 12.89, k1 is practically constant, whereas it chromogen peak “D” that gives an isobestic point at
increases progressively at pH ≥12.89. Anbar and Yagil λ1 = 290 nm and a pseudoisobestic point at λ2 =
[8] first established that the catalytic effect of OH− ions 234 nm. These two points mean that the disappearance
could be explained considering the partial dissociation of NH2 Cl and the formation of D are simultaneous.
of NH2 Cl into chloramide NHCl− ion (pKaNH2 Cl =
18). They compared the relative rates of the reaction of k3
ν1 NH2 Cl+ν2 HEH −→ ν3 D
ammonia, mono-, di-, and triamine in alkaline medium
with NH2 Cl. These rates increase sharply with the After a longer period, UV analysis showed that the ab-
degree of amine substitution. On the contrary, they sorption bands do not pass through the isobestic points
noted the absence of any diminution of the rate when and that, finally, a new isobestic point appears at λ3 =
NH2 Cl was substituted. Previous works of our lab- 247 nm. At this point, only two products were present
oratory [9,10] confirmed these results and permitted in the medium, D, and a new peak F at λ = 224 nm. The
establishing the following reaction scheme: NH2 Cl was totally consumed. The chromogen products
D and F are linked together by the relation
NH2 Cl + HO-(CH2 )2 -NH2
k4
ν3 D −→ ν4 F
→ HO-(CH2 )2 -NH-NH2 + HCl
NH2 Cl NHCl− + H+ To characterize the two processes, GC–MS analyses
were carried out. The initial concentrations for NH2 Cl,
HO-(CH2 )2 -NH2 + NHCl− HEH, and NaOH were equal to 0.1, 0.11, and 0.5 M,
→ HO-(CH2 )2 -NH-NH2 + Cl− (6) respectively, which corresponds to HEH/NH2 Cl, and
NaOH/NH2 Cl ratios almost equal to 1.1 and 5.
The concentrations were a little higher than the re-
This reaction scheme is in accordance with the fact that
action medium, to obtain sufficient sensitivity for the
NH2 Cl reacts with trimethylamine to give a salt and, as
analyses.
this reaction is also catalyzed by the OH− ions [8–11],
After 10 min reaction, the GC–MS spectrum shows
we obtain
that residual HEH was observed at t2 = 4.8 min and
a bulky peak located at t1 = 3 min corresponds to the
(CH3 )3 N + NH2 Cl → (CH3 )3 NNH+
2 Cl
−
reaction product. GC–MS analysis gives a mass of m/z
(basic catalysis) = 74 for this product. Also, the fragmentation analysis
gives the formula
Characterization of the Products. The reaction sys- that is, the hydroxyethylhydrazone. Its functional
tem HEH/NH2 Cl was studied either by UV or by group corresponds to the UV peak of product F at
HPLC, and the reaction products were characterized λ = 224 nm.
by GC–MS. In addition, the experiments were carried
out at pH 12.89 and T = 25◦ C and for HEH concen- Reaction Mechanisms. By analogy with the phe-
trations between 8 and 40 × 10−3 M. nomena observed in our laboratory in the case
Figure 3 UV spectra for a reaction mixture HEH + NH2 Cl at 25◦ C. [HEH]0 = 40 × 10−3 M; [NH2 Cl]0 = 1.6 × 10−3 M;
[NaOH]0 = 0.1M. The first trace was recorded at 2 min and then at every 5 min. [Color figure can be viewed in the online issue,
which is available at wileyonlinelibrary.com.]
T = 25◦ C, [NH2 Cl]0 = 1.7 × 10−3 M, [HEH]0 = 40 × 10−3 M, [NaOH] = 0.1 M with A = ([NH2 Cl]0 × [HEH])/([HEH]0 × [NH2 Cl]).
resolution of the following differential equations: culate the global composition of the reaction mixture
at t = 0, noted Ci (i = 1–5), after the injection of the
dx reagents, and at t = ∞, noted Di (i = 2–5).
= −k1 a x − k3 u x − k2 xb0
dt To achieve this, the volumes of NH2 Cl and EA to
da be injected are designated by VN and VA , respectively:
= −k1 a x
dt
B1
du VN = 1000 mL, VA = 103 × p ×
= k1 a x − k3 u x CA
dt
df where subscript A represents an EA solution with mass
= k3 u x
dt composition WA :
Figure 6 Kinetic profile at T = 20 and 80◦ C with [NH2 Cl]0 = 0.42 M, [EA]0 = 8.47 M. T = 80◦ C: (a) [NH2 Cl]; (b) [HEH];
(c) [hydrazone]. T = 20◦ C: (a ) [NH2 Cl]: (b ) [HEH]; (c ) [hydrazone].
Thus, the situation is reversed for their electrophilic Thus kf (Raschig) ≈ kf (CH2 OCH2 ) ≈ 103 kf
homologue. (CletOH)
The N-Cl linkage of NH2 Cl is not very polarized due
to the very slight electronegative difference between
the two atoms. This explains the polarization inversion
when a hydrogen atom is replaced by an electrodonor HEH Reaction Mechanisms and Degradation and
methyl group. This substituted chloramine becomes Alkylation Rates. For identical reagent ratios, the
incapable of forming N-N linkage by reacting with HEH yields are the same for the two alkylation meth-
NH3 in an aqueous or anhydrous medium (chlorine ods (CletOH and CH2 OCH2 ). This result is not sur-
transfer mechanism in liquid ammonia). prising because the rate constants kf and kd require
the same mechanisms. This is confirmed by acti-
δ+ δ− δ− δ+
NH2 -Cl CH3 NH - Cl vation enthalpies and entropies. The absolute for-
mation rates are very different (Vf (CH2 OCH2 ) Vf
This is not the case of the epoxide, which is strongly (CletOH)), but the kf /kd ratios are almost identi-
electrophilic, due to its favorable spatial configuration cal. The adjustment variable, that is, ratio [N2 H4 ]0 /
(flat molecule, symmetry, and good site accessibility) [CH2 OCH2 ]0 or [N2 H4 ]0 /[CletOH]0 , will be low, close
and to greater carbon–oxygen polarization. to three, to obtain rates up to 80%.
The very weak value of the direct alkylation con- In the case of the Raschig process, the secondary re-
stant by CletOH in comparison with CH2 OCH2 , can be action of dialkylation is replaced by an HEH oxidation
explained by the fact that the carbon–chlorine linkage process; the reaction mechanism of which is different
is less polarized and accessible:
δ+1/2 δ+1/2
N2H4 + HEH (k = 1.71 × 10 L mol s at 25°C)
O δ
δ δ+
N2H4 + Cl-CH2-CH2-OH HEH (k = 2.18 × 10 L mol s at 25°C)
kdegradation HEH /
from the formation mechanism (SN2 ). Since the bi-
kformation HEH
T = 25◦ C
molecular rate constants in favor of degradation are
13.6
0.7
0.7
equal to 14, the adjustment variable [EA]0 /[NH2 Cl]0
will be at least higher than 20.
ki at T = 25◦ C
Rate Constant
(L mol−1 s−1 )
−102
−127
−128
formation.
Si0#
−89
55.0
45.2
79.0
75.7
50.8
51.6
3.06 × 107
7.95 × 106
4.04 × 108
8.05 × 107
3.74 × 106
3.46 × 106
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