C. D. Derby et al.
With l-lysine as substrate, the appKm value at pH 5 is
ꢀ0.8 mm. Assuming that 1 mg of escapin that is released in
ꢀ1 mL (i.e., the amount released during a bout of inking) is
combined with 145 mm l-lysine (i.e., its concentration in
opaline), then escapin is more than 99% saturated with the
substrate. Under these conditions, enzymatic turnover of es-
capin with l-lysine would take as little as ꢀ5 s to produce
1 mm H2O2 and ꢀ30 s to produce ꢀ5 mm H2O2. At higher
pH values, the reactions are even faster. For example, at
pH 8, it would take less than 1 s to produce 1 mm H2O2 and
ꢀ1 min to produce ꢀ80 mm H2O2. Thus, escapin remains
active at the naturally low pH of ink, and owing to the high
concentrations of escapin and lysine in the defensive secre-
tion, prodigious amounts of its reaction products are pro-
duced.
with the blunt end of a scalpel handle. Escapin was isolated and purified
using an ꢂKTA 100 Automated FPLC. A two-step purification process
involving gel filtration followed by purification using cation exchange
was performed according to Yang et al.[10]
Preparation of the intermediate products of escapinꢀs oxidation of l-
lysine: The method of Meister (1952) was modified to make “escapin in-
termediate product for l-lysine” (EIP). l-Lysine monohydrochloride
(10 mg) was incubated with escapin (3 mg) and catalase (130 mg) in
double distilled H2O (1 mL) at 308C on a shaker for up to 20–24 h until
l-lysine was completely consumed, as determined by thin layer chroma-
tography. This solution was then filtered using an Amicon Ultra-4 Centri-
fugal Filter Device (Millipore Corp., Billerica, MA, USA) to remove es-
capin and catalase, and then stored at ꢁ808C until used later. To make
“escapin end product for l-lysine” (EEP), the same procedure was per-
formed except that catalase was not included in the incubation and con-
centration of escapin (0.6 mg) in H2O mL. All chemicals were purchased
from Sigma–Aldrich (St. Louis, MO, USA).
Spectroscopy: NMR spectra were recorded on a Bruker Avance 400
NMR spectrometer using conventional pulse sequence, and FID data
were processed using MestRe Nova software (Mestrelab Research) on
Windows XP. 10% D2O/90% H2O was used as solvent for all experi-
ments except that in Scheme 2b, bottom spectrum. Chemical shift was
referenced for internal TSP. Mass spectra (ESI) were obtained using a
Waters Q-TOF micro mass spectrometer and Applied Biosystems
QSTAR XL.
Conclusions
The mixture resulting from the escapin/lysine reaction in the
ink secretion of sea hares is complex. It is generated by an
initial enzymatic step that generates an equilibrium mixture
of components, and followed by non-enzymatic reactions be-
tween these components and H2O2. The balance within the
equilibrium mixture is dependent on the mixtureꢀs pH,
which ranges from ꢀ5 in full strength ink to ~8 when dilut-
ed in sea water. The enzymatic step of the escapin pathway
generates D1-piperidine-2-carboxylic acid (3) and H2O2 as
the major components, regardless of the pH value. Minor
forms include a-keto-e-aminocaproic acid (2), 6-amino-2-hy-
droxy-hex-2-enoic acid (7), and aminol 2-hydroxy-piperi-
dine-2-carboxylic acid (9), which increase in abundance at
lower pH, and D2-piperidine-2-carboxylic acid (4), which in-
creases in abundance at higher pH. The non-enzymatic reac-
tion of H2O2 with these intermediate forms results in the
end products d-aminovaleric acid (5) and d-valerolactam
(6), with 6 dominating under all pH conditions but the rela-
tive abundance of the latter increasing under acidic condi-
tions. The complexity of the mixture generated by escapin in
aqueous solution is greater than previously realized for any
l-amino acid oxidase. The pH effect on the equilibrium in
EIP and on the production of end products shows that pH
affects the activity of EIP and EEP. Our results with escapin
may indicate equally complex mixtures are generated by
other l-lysine oxidases. The products of the escapin pathway
can now be tested in biological assays to determine which
are antipredatory chemical defenses or antimicrobial agents.
Enzyme kinetics and pH profiles: Enzyme activity was measured in air-
saturated 50 mm potassium phosphate, 150 mm NaCl, in the pH range
from 4.5 to 8.5, at 258C, by monitoring the rate of oxygen consumption
with a computer-interfaced Oxy-32 oxygen monitoring system (Hansa-
tech Instrument, Ltd.). The reactions were started by the addition of es-
capin to a 1 mL reaction mixture, with the final concentration of enzyme
in the 5 to 20 mgmLꢁ1. At any given pH, the final concentrations of l-
lysine spanned from 0.2- to 5-times the appKm values, which corresponded
to 0.01 to 7 mm depending upon the pH. Data were fit with Kaleida-
Graph software (Synergy Software, Reading, PA). The apparent kinetic
app
parameters
V
max
, ACHTUNGRTENNUNG
app(Vmax/Km), and appKm for l-lysine as substrate for es-
capin in air-saturated buffers were determined by fitting initial rates of
reaction at different concentrations of substrate to the Michaelis–Menten
app
equation for one substrate. The pH dependence of the
V
and
max
app(Vmax/Km) values were determined by fitting initial rate data to equa-
ACHTUNGTRENNUNG
tion 1, which describes a curve with a slope of +1 and a plateau region
at high pH. Y is the pH-independent value of the kinetic parameter of in-
terest, and Ka is the dissociation constant for the ionization of groups
which are relevant for catalysis.
!
Y
10ꢁpH
10ꢁpKa
log Y ¼ log
ꢀ
ꢁ
ð1Þ
1 þ
Conversion of EIP to EEP at different pH values: Potassium phosphate
buffer was used as the incubation solution for the conversion of EIP to
EEP, since the type of buffer affected the results. Freeze-dried EIP
(2.5 mg, 13.7 mmol lysine equivalent) and H2O2 (50 mmol in 5.6 mL of
30% solution) were mixed with 100 mm potassium phosphate buffer and
adjusted pH to 6, 7, and 8 to a final volume of 0.5 mL. Reactions were
performed for 1.5 h at 258C (Thermomixer, Eppendorf), and products
were analyzed using NMR. For high resolution mass spectroscopy, com-
pound
5 and 6 were purified by Beckman HPLC System GOLD
equipped with Nomura Chemical Develosil RPAQUEOUS column.
Water - methanol gradient containing 0.1% trifluoroacetic acid was used
for elution of the compounds.
Experimental Section
Animals: Sea hares Aplysia californica Cooper 1863 were collected in
California by Marinus Scientific (Garden Grove, CA, USA). They were
dissected on the day of arrival in our laboratory. Experiments were per-
formed within the university regulations and national guidelines.
Acknowledgements
Collection of ink and isolation of escapin: The ink glands were dissected
from anesthetized animals and frozen at ꢁ808C until used. Purple ink
was collected by gently squeezing dissected ink glands in a Petri dish
Supported by NSF IBN-0324435 and 0614685 (to C.D.D.), NIH GM-
34766 (to P.C.T.), NSF MCB-0545712 and American Chemical Society
1602
ꢁ 2009 Wiley-VCH Verlag GmbH & Co. KGaA, Weinheim
Chem. Eur. J. 2009, 15, 1597 – 1603