The Journal of Organic Chemistry
Article
This observation shows strong parallels with the accelerated
Table 2. Screening of Liquid-Assisted Grinding and One-
Pot Two-Step Process
37
a
̌
̌
́
aging, described by Friscic et al. For comparison, the
conventional liquid-phase synthesis already shows HAT-CN
formed after the coupling in refluxing acetic acid (cf.
different mechanistic pathway of the mechanochemical and the
liquid-phase synthesis.
entry
LAG additive
LAG amount [η]
yield [%]
1
2
3
4
5
6
7
8
9
48
0
H2O
H2O
H2O
methanol
ethanol
toluol
DCM
DMF
H2O
0.2
0.1
0.05
0.1
0.1
0.1
0.1
0.1
0.1
67
62
45
50
29
36
19
47
0
Overall, we were able to significantly improve the synthesis
of HAT-CN by performing the condensation reaction in as
little as 10 min inside a ball mill. Thus, making it significantly
more sustainable by completely avoiding acetic acid and
acetonitrile. The use of water as a liquid-assisted grinding
additive led to a yield of up to 67%, significantly outperforming
the state of the art. To further enhance the environmental
compatibility, we conducted the reaction without any excess
diaminomaleonitrile, leading to less product but overall better
green metrics. The product mass intensity is lower by a factor
of up to 795. With our synthetic pathway, 78% CO2
equivalents can be saved. Our synthetic approach does not
rely on high excesses of one starting material, solvents, or high
temperatures and, therefore, is more cost- and time-efficient
than the traditional way, while giving improved yields.
b
10
11
c
a
All approaches were milled for 10 min at 35 Hz in a 10 mL ZrO2 vial
containing 0.40 g of hexaketocyclohexane, 1.10 g of diaminomaleoni-
b
trile, and 1 Ø = 10 mm ZrO2 milling ball. 0.42 g of
c
diaminomaleonitrile (stoichiometric amount) was used After the
first step, the solution workup was replaced by adding 1 mL of 30%
HNO3 (9.36 mmol) to the milling vessel and milling the mixture for
another 10 min at 30 Hz.
as water (Table 2, entries 5 and 6). Water appears to be a
critical additive, which may function as a stabilizing agent.
Switching to common, aprotic organic solvents like DCM and
toluene (Table 2, entries 7 and 8), the yields are lowered
drastically, supporting the suspicion that the water is involved
in the reaction not as a solvent, as the solubility of both starting
materials in water is poor compared to the other used LAG
additives. Using DMF as an additive led to a drastic decrease in
conversion, which might be because of side reactions.
Therefore, we could conclude that polar protic solvents are
beneficial for this condensation reaction.
EXPERIMENTAL SECTION
■
General Information. All reagents were obtained from
commercial suppliers and were used without purification. Acids and
solvents for the LAG were used in the anhydrous form if not
mentioned otherwise. Water used in LAG was taken from a tap for the
deionized form. The mechanochemical step was carried out in a
Retsch MM400 and Retsch MM500 nano/vario ball mill. Commercial
milling vessels out of zirconium dioxide were used. Zirconium dioxide
(Type ZY-S) milling balls with a diameter of 10 mm were purchased
from Sigmund Lindner GmbH. The average weight of one milling ball
is 3.19
0.05 g. Nuclear magnetic resonance spectroscopy was
recorded on a Bruker BRUKER Avance III HD 300 MHz NMR
spectrometer. As a solvent and internal standard, acetone-d6 was used.
Fourier transform infrared spectroscopy (FT-IR) was carried out on a
SHIMADZU IR Spirit with a QATR-S ATR unit. Each sample was
measured with 15 scans with a resolution of 4 in the range from 400
to 4000 cm−1. Elemental analysis was carried out on a vario Micro
cube from Elementar Analysensysteme GmbH at 1200 °C. Raman
spectra were obtained using a RENISHAW inVia Qontor Raman
microscope with 50× object (NA = 0.50, 8.2 mm free working
distance). The wavelength for the measurement was 785 nm with
0.001−10% laser power dependent on the sample. The exposure time
varied between 20s and 2 accumulations and 1s and 20
accumulations, of which the latter resulted in the best spectra.
Synthesis of 1,4,5,8,9,11-Hexaazatriphenylenehexacarbo-
nitrile. In a typical synthesis, the reactants were placed in a 10 mL
ZrO2 milling vial together with a Ø = 10 mm ZrO2 milling ball. Then,
0.400 g (1.30 mmol, 1 equiv) of hexaketocyclohexane-octahydrate,
1.10 g (10.20 mmol, 7,84 equiv) of diaminomaleonitrile and the
respective additives were added (for detailed information, see section
at 35 Hz in a Retsch MM500 mixer ball mill (MBM). After the
milling, the raw mixture was transferred into a flask and stirred in 30%
HNO3 in a 110 °C oil bath for an hour. After cooling, the orange-solid
HAT-CN was filtered, washed with water, and dried. An evenly bright
yellow solid was isolated (0.3319 g, 0.864 mmol) in 67% yield.
13C{1H} NMR (300 MHz, CO(CD3)2): δ 143.4, 136.6, 114.4 ppm.
To verify the merit of our approach in terms of
sustainability, we calculated the green metrics (cf. Supporting
Information, section 3). The stoichiometric approach has a
795-times better mass productivity and process mass intensity
compared to the solution-based protocol. In addition, the
reaction time is strongly reduced, and thus, the global warming
potential of the process can be reduced by 78%. Overall, the
sustainability of the reaction has been vastly increased by the
use of mechanochemistry.
Analogously to the conventional route, the presented
synthesis also involves a workup with HNO3. As reported for
the conventional route, this serves as a purification step to
dissolve unreacted or incompletely reacted (1- or 2-fold
condensation, excess diaminomaleonitrile) reaction products.
We attempted to substitute this liquid phase workup with a
second treatment inside the ball mill. Oxidizing agents like
potassium peroxymonosulfate, sodium perchlorate, sodium
percarbonate, or liquid HNO3 (Table 2, entry 11 and Table
S2) were employed in a one-pot two-step process, but no
product could be isolated for any of them. In the
mechanochemical approach, however, this treatment is crucial
for another reason. As our analysis shows that no HAT-CN but
an intermediate is formed during the milling process. This
intermediate must be an adduct of the two starting materials in
a precoordinated fashion, as the starting materials themselves
are not stable under 30% HNO3 conditions (for a detailed
intermediate is exposed to the same conditions, however, it is
transferred into HAT-CN and precipitating from the solution.
FT-IR: ν 2240, 1340, 1226, 1146 cm−1. Raman: ν 2253, 1400, 1480,
1540, 700 cm−1. HRMS (MALDI-TOF, TCNQ): M+ 384.7 m/z.
Elemental analysis: 54.6%, C; 43.1%, N; 0.4%, H; 0%, S. The melting
point is reported to be >500 °C and was not further explored for
analysis.
Upscaling the Synthesis of 1,4,5,8,9,11-Hexaazatriphenyle-
nehexacarbo-nitrile in the MM-500. To check the scalability of
C
J. Org. Chem. XXXX, XXX, XXX−XXX