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CounterCurrent Separation
Theory	and	practice
§Minimal sample preparation
(direct chromatography of crude extracts)
§High mass – High resolution
§No sample loss (support-free
chromatography)
§Reproducibility
(scale-up or scale down)
§Flexibility
§Mild conditions for sensitive molecules
How	does	a	separatory funnel	work?
Liquid- Liquid	Extraction
2.	Add	compound	mixture	(solutes)
3.	Shake	(vigorous	mixing	of	phases)
4.	Allow	phases	to	separate	(settling)
5.	Physically	separate	layers
1.	Formulate	biphasic	solvent	mixture	(system)
Solvent	System	=	SS Phase	System
6.	Analyze	layers	for	composition
Liquid- Liquid	Extraction
Simple	biphasic	solvent	systems	are	created	by	
mixing	two	immiscible	liquids.
Organic/Aqueous
liquid/liquid separation
Biphasic	solvent	systems	may	have	2	or	more	solvents.
Liquid- Liquid	Extraction
A	common	way	of	formulating	solvent	system	is	to	start	with	2	
immiscible	solvents	and	add	one	or	more	modifiers.
Chloroform/Water
Chloroform/Methanol/Water (ChMWat)
Hexane/Water
Hexane/Methanol/Water
Hexane/	Ethyl	Acetate /Water
Hexane/ Ethyl	Acetate /Methanol/Water HEMWat
Survey	Results
23
133
223
10
3
2
3
4
5
6
number	of	solvents
number	of	solvents	per	SS
Friesen	2015	J	Nat	Prod		v.	78	p.	1764
Liquid- Liquid	Extraction
Ternary	Phase	Diagrams	(for	three-component	solvent	systems)
Liquid- Liquid	Extraction
Solvent	System	Characterization
Berthod,	A.	(2002).	Countercurrent	Chromatography:	The	support-free	liquid	stationary	phase.	Wilson	&	Wilson's	Comprehensive	
Analytical	Chemistry	Vol.	38.	Boston:	Elsevier	Science	Ltd.	pp.	1–397.	ISBN	978-0-444-50737-2.
Fig.	3.	(a)	Chemical	structure	of	benzotrifluoride and	(b)	ternary	phase	diagram	of	n-
hexane/benzotrifluoride/acetonitrile	with	two-phase	region	at	22◩C	shown	in	grey	
shading.	Volumetric	solvent	composition	for	the	CCC	separation	is	represented	as	
ared triangle	(50%	n-hexane,	17.5%	benzotrifluoride,	32.5%	acetonitrile,	
10:3.5:6.5).The	tie-lines	indicate	that	benzotrifluoride partitioned	evenly	between	n-
hexane	and	acetonitrile.	The	composition	of	the	upper	and	lower	phases	varied	
extensively	with	the	amount	of	benzotrifluoride in	the	system
J	Chromatogr A.	2015	Apr	3;1388:119-25.	doi:	10.1016/j.chroma.2015.02.020.	
Isolation	of	ÎČ-carotene,	α-carotene	and	lutein	from	carrots	by	countercurrent	chromatography	with	the	solvent	
system	modifier	benzotrifluoride.	Englert M,	Hammann S,	Vetter	W.
Solvent	System	Characterization
Liquid- Liquid	Extraction
Biphasic	solvent	systems	created	by	mixing	two	
or	more	immiscible	liquids.
Alcohol/Ionic	Aqueous or	Acetonitrile/Ionic	Aqueous
Aqueous	Two	Phase	Solvent	Systems	(ATPS)
Polyethylene	Glycol/Buffered	Aqueous
Organic/Organic or	“non-aqueous”	(heptane/methanol)
Organic/Aqueous (ChMWat,	HEMWat,	etc
)
Unified	Solvent	Notation
Petroleum	ether Pet DMSO So
Hexane H Acetonitrile Ac
Heptane Hep Isopropyl alcohol Iso
Cyclohexane Cy n-propanol Pro
Toluene Tol n-butanol Bu
Methyl tert-butylether ter Acetic	acid Aa
THF Tet Ethanol Et
Diethyl	ether De Methanol M
Ethyl	acetate E Water Wat
Methyl	acetate Me
Chloroform Ch
Dichloromethane Di
Acetone At
1. Solvent	Abbreviations	
Used	Define	Countercurrent	Separation	Solvent Systems
Unified	Solvent	System	Notation
2.	Order	of	polarity:	least	polar	to	most	polar		Ă  HEMWat,	ChMWat,	terBuAcWat
4.	Whole	numbers		Ă  HEMWat 2:3:4:5
4a.	No	numbers	needed	for	binary	solvent	systems
5b.	Lowest	common	denominator?		5:5:5:5	or	1:1:1:1
6.	pre-equilibration	additives/modifiers	in	parentheses	Ă  terBuAcWat (0.7%	TFA)
6a.	What	does	concentration	mean?	
Concentration	in	a	single	component	or	overall	mixture?
3.	Volume	ratios	Ă  HEMWat 2:3:4:5
6b.	Modifier	or	solvent	component?	acetic	acid,	ionic	liquids,	
1. Solvent	abbreviations	
1a.	Write	out	new	or	rare	solvents
7.	pH-zone	refining	and	Ion-exchange	(retainer	- eluter)
HEMWat
http://2.bp.blogspot.com/-4jotcEHY_Iw/Tu7oPvHVX9I/AAAAAAAAAyk/fsircQR9n3A/s1600/workhorse_discing.jpg
The	HEMWat SS	Family
Biphasic	solvent	systems	created	by	mixing	two	or	more	immiscible	liquids.
organic/organic	modifier/aqueous	modifier/aqueous
+	low-cost
+	versatile	and	tunable	(heptane	or	pet	ether		or	limonene	for	hexane)
(ethanol	for	methanol)
+	good	CCC/CPC	performance	(high	Sf values)
Hexane/ Ethyl	Acetate /Methanol/Water		= HEMWat
- environmental	impact	/	health	concerns
- stability
- what	about	pH,	shouldn’t	we	buffer	this?
+	create	solvent	system	families by	systematic	modification
The	HEMWat SS	Family
HEMWat solvent composition
0%
25%
50%
75%
100%
+8 +7 +6 +5 +4 +3 +2 +1 0 -1 -2 -3 -4 -5 -6 -7 -8
HEMWat number
Hexane
EtOAc
MeOH
Water
Friesen	B	&	Pauli	GF
G.U.E.S.S.	to	make	Generally	Useful	Estimations	of	Solvent	Systems	in	CCC.
Journal	of	Liquid	Chromatography	&	Relat.	Technologies	28:	2777-2806	(2005)
dx.doi.org/10.1080/10826070500225234
The	HEMWat SS	Family
Oka	F,	Oka	H,	Ito	Y	(1991)	J	Chromatogr A	538:99–105
Anal Bioanal Chem. 2005 Sep;383(2):327-340.
Alkane effect in the Arizona liquid systems used in countercurrent chromatography.
Berthod A1, Hassoun M, Ruiz-Angel MJ.
10.1007/s00216-005-0016-7
The	HEMWat SS	Family
Renault	JH,	Nuzillard JM,	Intes O,	Maciuk A	(2002)	In:	Berthod A	(ed)	Countercurrent	
chromatography,	the	support	free	liquid	stationary	phase	(Comprehensive	analytical	chemistry,	
vol.	38).	Elsevier,	Amsterdam,	pp	49–83
The	HEMWatSS	family
The	HEMWat SS	Family
Dubant S, Mathews B, Higginson P, Crook R, Snowden M, Mitchell J. Practical
solvent system selection for counter-current separation of pharmaceutical
compounds. J Chromatogr A 2008; 1207: 190–192
The	HEMWat SS	family
A	novel	9	× 9	map-based	solvent	selection	strategy	for	targeted	counter-current	chromatography	isolation	of	natural	productsOriginal Research	Article
Journal	of	Chromatography	A,	Volume	1400,	26	June	2015,	Pages	27-39
Junling Liang,	Jie Meng,	Dingfang Wu,	Mengzhe Guo,	Shihua Wu			doi:10.1016/j.chroma.2015.04.043
The	HEMWat SS	Family
8	x	8	=	64	possibilitiesThe	HEMWat SS	family
The	HEMWat SS	Family
J	Chromatogr A.	2014	Nov	14;1368:116-24.	doi:	10.1016/j.chroma.2014.09.064.	Folding	fan	mode	counter-current	chromatography	offers	fast	
blind	screening	for	drug	discovery.	Case	study:	finding	anti-enterovirus	71	agents	from	Anemarrhena asphodeloides.
Liu	M,	Tao	L,	Chau	SL,	Wu	R,	Zhang	H,	Yang	Y,	Yang	D,	Bian Z,	Lu	A,	Han	Q,	Xu	H8.
461
261
232
172
104
42
35
33
24
23
22
18
8
5
3
2
2
1
water
ethyl	acetate
methanol
hexane
n-butanol
acetonitrile
ethanol
chloroform
pet	ether
heptane
methyl	t-butyl	ether
isopropanol
dichloromethane
acetone
ethyl	ether
cyclohexane
carbon	tetrachloride
THF
Survey	Results
Friesen2015_JNP_78_1764_countercurrent
Solvents	used	in	Biphasic	SSs
97%	had	water
35%	HEMWat
16%	similar	to	HEMWat
The	HEMWat SS	Family
Solvent	System	Properties
http://us.hola.com/imagenes/viajes/2011071553613/chicago-moderno-estados-unidos/0-181-586/a_009GenSM-a.jpg
Solvent	System	Properties	
Polarity
Selectivity
Friesen,	J.	B.;	Ahmed,	S.;	Pauli,	G.	F.	Qualitative	and	quantitative	evaluation	of	solvent	systems	for	countercurrent	separation.	Journal	of	
Chromatography	A 2015,	1377,	55–63	DOI:	10.1016/j.chroma.2014.11.085.
Will	my	chromatography	method	position	the	target	
compounds	with	a	reasonable	VR (tR)?
Not	in	void	volume.
Not	highly	retained	on	the	column
Can	molecules	with	similar	polarity	be	separated	in	
that	region	with	a	reasonable	VR?
match	between	solvent	system	and	solute	(polarity	scales	such	as	LogPo/w	,
Reichardt’s Dye	scale,	and	eluotropic sequences )
Polarity
1. (Linear	combination	of)	
Eluotropic sequence	parameters
2.	Solvatochromic (Reichardt’s)	Dye
3.	GUESSmix method
4.	Phase	Metering	Apparatus
(Linear	combination	of)	Eluotropic sequence	parameters
Journal	of	Chromatography	A	Volume	1393,	8	May	2015,	Pages	47–56	Systematic	and	practical	solvent	system	selection	strategy	based	on	the	nonrandom	two-liquid	segment	
activity	coefficient	model	for	real-life	counter-current	chromatography	separation	Da-Bing	Ren,	Lun-Zhao	Yi,	Yan-Hua	Qin,	Yong-Huan Yun,	Bai-Chuan Deng,	Hong-Mei	Lu,	Xiao-
Qing	Chen,	Yi-Zeng	Liang,
Journal	of	Chromatography	A	Volume	1393,	8	May	2015,	Pages	47–56	Systematic	and	practical	solvent	system	selection	strategy	based	on	the	nonrandom	two-liquid	segment	
activity	coefficient	model	for	real-life	counter-current	chromatography	separation	Da-Bing	Ren,	Lun-Zhao	Yi,	Yan-Hua	Qin,	Yong-Huan Yun,	Bai-Chuan Deng,	Hong-Mei	Lu,	Xiao-
Qing	Chen,	Yi-Zeng	Liang,	
(Linear	combination	of)	Eluotropic sequence	parameters
Solvent X Y- Y+ Z
acetonitrile 0.018 0.131 0.883 0.000
chloroform, 0.393 0.0 0.167 0.000
ethyl acetate 0.3339 0.058 0.441 0.000
ethanol 0.251 0.030 0.000 0.630
n-butanol 0.425 0.004 0.0 0.490
methanol 0.090 0.139 0.0 0.594
methyl tert-butyl ether 0.483 0.105 0.142 0.000
hexane 1.000 0.000 0.000 0.000
heptane 1.152 0.000 0.000 0.000
water 0.000 0.000 0.000 1.000
Table S1. The NRTL-SAC parameters of the used solvents in this work.
Journal	of	Chromatography	A	Volume	1393,	8	May	2015,	Pages	47–56	Systematic	and	practical	solvent	system	selection	strategy	based	on	the	nonrandom	two-liquid	segment	
activity	coefficient	model	for	real-life	counter-current	chromatography	separation	Da-Bing	Ren,	Lun-Zhao	Yi,	Yan-Hua	Qin,	Yong-Huan Yun,	Bai-Chuan Deng,	Hong-Mei	Lu,	Xiao-
Qing	Chen,	Yi-Zeng	Liang,	
Solute X Y- Y+ Z
Nicotinic acid 0.093 0.000 0.272 0.588
3,4-dihydroxybenzoic acid 0.338 0.728 0.708 0.742
Chlorogenic acid 0.142 1.074 1.086 1.416
Antipyrine 0.112 0.220 0.446 0.594
(Linear	combination	of)	Eluotropic sequence	parameters
Polarity
Polarity
2.	Solvatochromic (Reichardt’s)	Dye
Hexanes														 Toluene																			t-BME																			Limonene													Dichloromethane
Dichloromethane			Ethyl	Acetate									 Acetone																					n-Butaniol Isopropanol
Isopropanol Acetonitrile Ethanol																					Methanol										Water
Solvatochromic (Reichardt’s)	Dye
https://upload.wikimedia.org/wikipedia/commons/thumb/2/28/Reichardt_dye_structure.svg/220px-Reichardt_dye_structure.svg.png
Solvatochromic (Reichardt’s)	Dye
400
500
600
wavelengthinnm
Upper Phase
Lower Phase
Reichardt’s dye lambda max values in the upper and lower phases of HEMWat solvent systems. Some
values could not be determined due to insufficient solubility of the dye.
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
500
600
wavelength	in	nm
Ch(Di)Mwat	Solvent	System
DiMWat
ChMWat
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Fig. 5. Reichardt’s dye lambda
max values in the lower phases of
ChMWat and DiMWat solvent
systems.
Solvatochromic (Reichardt’s)	Dye
Polarity
3.	GUESSmix
Model Compounds:
HO
H
H H
H
O
O
OH
OH
O
O O
HO
H H
H
CH3
OH
OH O
OHO
OH
N
O
OH
O
OH
O
HO
O
O
OH
O OHO
O
H
HO
H
HO
H
H
OHH
O
OH
OH
O
OH
O
O
OH OH
OH
O
O
OH
OH
HO
O
O
H
HO
H
HO
H
H
OHH
O
OH
OH
N
N
N
N
O
O
N
H
O
OH
NH2
N
N
OH
S
O
O
O
SO
O
O
S
O
O
O
3Na
N
H
N
O
OH
H
H
O
O
O
O
O
O
O
O
OH
OH
OH
OOH
HO
The GUESSmix
Friesen J.B, Pauli G.F. Journal of Liquid
Chromatography and Related Technologies, 28:
2777-2806, 2005
b
O
Q
r
R
U
F
Y
C
I
E
MZ
V
G
T X
H
D
N
A
Solvent	Systems	Surveyed
hexane
ethyl	
acetate
methanol
chloroform
dichloromethane
water
methyl
t-butyl
ether
ACN
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
GUESSmix polarity	index	(GUPI)
0
10
20
HepM	10:10
HterAcWat	8:2:8:2
HBuMWat	5:5:5:5
HEMWat	7:3:6:4
HEMWat	8:2:8:2
HEMWat	5:5:5:5
terBuMWat	5:5:5:5
HEMWat	4:6:4:6
DiMWat*	10:7:3
DiMWat*	10:6:4
terAcWat	7:3:10
terAcWat	7:6:7
HterAcWat	3:7:3:7
HterAcWat	6:10:1:4
HEMWat	1:9:1:9
HEMWat	3:7:3:7
ChWat*	10:10
ChMWat*	10:6:4
ChMWat*	10:4:6
ChMWat*	10:2:8
DiWat*	10:10
DiMWat*	10:4:6
DiMWat*	10:2:8
terAcWat	5:5:5
terAcWat	5:5:10
EBuWat	8:2:10
HterAcWat	5:5:5:5
EBuWat	4:6:10
terAcWat	8:2:10
number	of	GUESSmix	compounds
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Fig.	1.	Graphic	representation	of	the	GUESSmix polarity	index	(GUPI)	of	the	solvent	systems	analyzed	in	this	study.	GUPI	is	the	
number	of	GUESSmix compounds	with	K	values	greater	than	1	divided	by	the	number	of	GUESSmix compounds	with	K	values	
less	than	or	equal	to	1	in	a	reversed-phase	elution	method	(aqueous	or	polar	phase	mobile).	*The	ChMWat and	DiMWat solvent	
systems	are	represented	as	the	inverse	of	the	original	K	values.
Polarity
4.	Phase	Metering	Apparatus
Phase	Metering	Apparatus
280000
280500
281000
281500
282000
282500
0 0.5 1 1.5 2
Log(Delectric	Constant	[literature	values])
Pauli	GF,	Pro	S,	Chadwick	L,	Burdick	T,	Pro	L,	Friedl W,	Novak,	N,	Maltby J,	Qiu,	F,	Friesen	JB	Real-Time	Volumetric	Phase	Monitoring	Advances	
Chemical	Analysis	by	Countercurrent	Separation	Analytical	Chemistry	87:7418-7425	(2015)
dx.doi.org/10.1021/acs.analchem.5b01613
Phase	Metering	Apparatus
300,500
302,500
304,500
2
PMA	
values
time	in	min
301,500
302,500
303,500
304,500
2 6
PMA	
values
time	in	min
HEMWat
5:5:5:5
UP
HEMWat
5:5:5:5
UP/LP
1:1
HEMWat
5:5:5:5
LP
HEMWat
5:5:5:5
LP
HEMWat
5:5:5:5
UP
Pauli	GF,	Pro	S,	Chadwick	L,	Burdick	T,	Pro	L,	Friedl W,	Novak,	N,	Maltby J,	Qiu,	F,	Friesen	JB	Real-Time	Volumetric	Phase	Monitoring	Advances	
Chemical	Analysis	by	Countercurrent	Separation	Analytical	Chemistry	87:7418-7425	(2015)
dx.doi.org/10.1021/acs.analchem.5b01613
Phase	Metering	Apparatus
300000
302000
304000
306000
upper
lower
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Phase	Metering	Apparatus
300950
301950
302950
303950
304950
ChMWat																																																																														DiMWat
	Upper
	Lower
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Phase	Metering	Apparatus
301900
302900
303900
HEMWat	10:0:10:0
HEMWat	9:1:9:1
HEMWat	8:2:8:2
HEMWat	7:3:7:3
HEMWat	7:3:6:4
HEMWat	6:4:6:4
HEMWat	7:3:5:5
HEMWat	6:4:5:5
HEMWat	5:5:5:5
HEMWat	4:6:5:5
HEMWat	3:7:5:5
HEMWat	4:6:4:6
HEMWat	3:7:4:6
HEMWat	3:7:3:7
HEMWat	2:8:2:8
HEMWat	1:9:1:9
HEMWat	0:10:0:10
ChMWat	10:0:10
ChMWat	10:1:9
ChMWat	10:2:8
ChMWat	10:3:7
ChMWat	10:4:6
ChMWat	10:5:5
ChMWat	10:6:4
ChMWat	10:7:3
DiMWat	10:0:10
DiMWat	10:1:9
DiMWat	10:2:8
DiMWat	10:3:7
DiMWat	10:4:6
DiMWat	10:5:5
DiMWat	10:6:4
DiMWat	10:7:3
EBuWat	10:0:10
EBuWat	8:2:10
EBuWat	6:4:10
EBuWat	4:6:10
EBuWat	2:8:10
EBuWat	0:10:10
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Fig. 3. Averages of the upper and lower phase permittivity
values measured by the phase metering apparatus for EBuWAt,
DiMWat, ChMWat, and HEMWat.
Selectivity
http://www.chocolati.com/new/images/P/24pcmix.jpg
Solvent	System	Properties
Selectivity
60
160
PW
PW+SS+PWSS
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Fig. 6. Selectivity parameters calculated for HEMWat solvent systems. Pairwise analysis calculated the ratio of K values for
every pairwise combination. A ratio of greater than 5/3 or less than 3/5 is considered to be adequate for the resolution of two
analytes. The number of resolved pairs is represented by αip. The number of GUESSmix analytes in the sweet spot is
represented by Nsw. The number of resolved pairs in the sweet spot is represented by αsw. The sum of these three
parameters (αip + Nsw + αsw), produced a selectivity score .
Selectivity
140
190
PW
PW+SS+PWSS
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Fig. 6. Selectivity parameters calculated for DiMWat solvent
systems. Pairwise analysis calculated the ratio of K values for
every pairwise combination. A ratio of greater than 5/3 or less
than 3/5 is considered to be adequate for the resolution of two
analytes. The number of resolved pairs is represented by αip.
The number of GUESSmix analytes in the sweet spot is
represented by Nsw. The number of resolved pairs in the
sweet spot is represented by αsw. The sum of these three
parameters (αip + Nsw + αsw), produced a selectivity score .
Selectivity
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Fig. 6. Selectivity parameters calculated for terAcWat solvent
systems. Pairwise analysis calculated the ratio of K values for
every pairwise combination. A ratio of greater than 5/3 or less
than 3/5 is considered to be adequate for the resolution of two
analytes. The number of resolved pairs is represented by αip.
The number of GUESSmix analytes in the sweet spot is
represented by Nsw. The number of resolved pairs in the
sweet spot is represented by αsw. The sum of these three
parameters (αip + Nsw + αsw), produced a selectivity score .
Polarity	and	Selectivity
2D		Reciprocal	(Shifted)	Symmetry	Plots
Mismatched	Polarity
Similar	Polarity	and	
Selectivity
2.7 4 8
8
2.7 4 8
8
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
Polarity	and	Selectivity
2D		Reciprocal	(Shifted)	Symmetry	Plots
Similar	Polarity	with	
Different	Selectivity
Development	and	
identification	of	orthogonal	
solvent	systems	is	the	key	to	
the	use	of	successive	
Countercurrent	Separation	
steps	in	purification.
2.7 4 8
8
Friesen	JB,	Ahmed	S,	Pauli	GF
Qualitative	and	Quantitative	Evaluation	of	Solvent	Systems	for	Countercurrent	Separation
Journal	of	Chromatography	A	1377:	55-63	(2015)
dx.doi.org/10.1016/j.chroma.2014.11.085
1
0
0.5
1
1.5
2
2.5
3
3.5
4
0 0.5 1 1.5 2 2.5 3 3.5 4
HBuMWat 5:5:5:5
HterAcWat5:5:5:5
2.7
4
8
8
2.7 4 8
8
ChMWat	10:7:3
DiMWat10:7:3
0
0.5
1
1.5
2
2.5
3
3.5
4
0 0.5 1 1.5 2 2.5 3 3.5 42.7 4 8
8
2.7
4
8
8
0
0.5
1
1.5
2
2.5
3
3.5
4
0 0.5 1 1.5 2 2.5 3 3.5 4
DiMWat10:6:4
HEMWat	4:6:4:6
2.7 4 8
8
2.7
4
8
8
R
C
V/A
M
E
Z
UN
F
Q
D
DiMwat10:6:4
HterAcwat 4:6:4:6
0
0.5
1
1.5
2
2.5
3
3.5
4
0 0.5 1 1.5 2 2.5 3 3.5 42.7 4 8
8
2.7
4
8
8
R
C
M
E
Z
U
Q
AV
N
F
D
A B
C D
GUESSmix Polarity	Matching
KD
interval
s
0
≀ KD <
0.0625
0.062
5
≀ KD <
0.125
0.125
≀ KD <
0.25
0.25
≀ KD <
0.5
0.5
≀ KD <
1
1
≀ KD <
2
2
≀ KD <
4
4
≀ KD <
8
8
≀ KD <
16
16
≀ KD <
32
32
≀ KD <
∞
-8
rXHTDC
GRFQUA
VNMEZ
OI Y b
-7
rXHTDC
GRFQUA
VNE
MZ O I Y b
-6
rXHTDC
GRFQUA
VNE
MZ O I Yb
-5
rXHTD
CGRAV
FQU
NE
MZ O I Yb
-4
rXHTD
CGR
AV
FQ
U
NE M Z O I Yb
-3
rXHTD
CGR
FQ
U
AVN E MZ O I Yb
-2
rXHTD
CGR
FQ
U
AVN ME Z O I Yb
-1
rXHTD
CG
RFQU AVN MEZ O I Yb
0 rXHTG DR CF
QUA
V
N ME Z O I Yb
KD
intervals
0
≀ KD <
0.0625
0.0625
≀ KD <
0.125
0.125
≀ KD <
0.25
0.25
≀ KD <
0.5
0.5
≀ KD <
1
1
≀ KD <
2
2
≀ KD <
4
4
≀ KD <
8
8
≀ KD <
16
16
≀ KD <
32
32
≀ KD <
∞
0
rXH
TG
DR CF
QUA
V
N ME Z O I Yb
+1
rXH
T
GR
DC
F
QUA
V
NM EZ O I Yb
+2 r XHT DCG RF
QUA
V
NM
EZ
O I Yb
+3 r XHT DCG RF
QUA
V
M
NE
Z
O IYb
+4
rXH
T
DCG RFU
QA
V
NM
EZ
O IYb
+5 r XHT DC G
RF
UA
V
M QZ
NEOIY
b
+6 r XHT D CG F
RU
AV
M Z
QNEO
IYb
+7 r XHT D CG F
RUA
V
MZ
QNEO
IYb
+8
rXH
T
D CG
FRUA
VM
Z
QNEO
IYb
Friesen	JB,	Pauli	GF.	Performance	characteristics	of	countercurrent	separation	in	analysis	of	natural	products	of	agricultural	significance.	J.	Agric.	Food	Chem.,	56,	19-28,	2008
EBuWat Solvent System Family
Ethyl Acetate / n-Butanol / Water
0
20
40
60
80
100
+5 +4 +3 +2 +1 0 -1 -2 -3 -4 -5
solvent system number
%
Ethyl Acetate
Butanol
Water
Solvent	System	Maps
Friesen, J.B. Pauli, G.F. Journal of Chromatography A 1151: 51-59 (2007)
Sweet Spot
FVAUMNE
RZQOIYb
GCDrTXH10:0:10
FVAUMNE
RZQOIYb
GDCXHTr8:2:10
FVAUMNE
RZQOIYb
GDCTXHr6:4:10
FVAUMNE
RZQOIYb
GCDTXHr4:6:10
FVAUMNE
RZQOIYb
GCDTXHr2:8:10
VAUMNER
ZQOIYb
FGCDTXHr0:10:10
32
≀ KD <
∞
16
≀ KD <
32
8
≀ KD <
16
4
≀ KD <
8
2
≀ KD <
4
1
≀ KD <
2
0.5
≀ KD <
1
0.25
≀ KD <
0.5
0.125
≀ KD <
0.25
0.062
5
≀ KD <
0.125
0
≀ KD <
0.0625
KD
intervals
Sweet Spot
EBuWat
KD
intervals
0
≀ KD <
0.0625
0.063
≀ KD <
0.125
0.125
≀ KD <
0.25
0.25
≀ KD <
0.5
0.5
≀ KD <
1
1
≀ KD <
2
2
≀ KD <
4
4
≀ KD <
8
8
≀ KD <
16
16
≀ KD <
32
32
≀ KD <
∞
HEMW
at 0
rXHTG DR CF QUAV N ME Z O I Yb
DEMW
at 0
rXHT G D C
FUV
A
RQ ZMNE OI Yb
DEMWat 0 (5:5:5:5)
HEMWat 0 (5:5:5:5)
FDR
A
O Yb
Z
E
M
NA
VU
X
H
T
G
r
C
Q
I
0 0.25 0.5 0.75 1 1.33 2 4 ∞K'(1)
∞
A
280nm
230nm
X
H
T
r
G
D
C
F
U
V
A
R
Q
ZMNE
OI
Yb
0 0.25 0.5 0.75 1 1.33 2 4K'(1)
SSMap
ReSPlotReSPlot
Pauli, G.; Pro, S.; Friesen, J. B.
Countercurrent Separation of Natural Products. J. Nat. Prod. 2008, 71, 1489-1508
terAcWat
system #
relative proportions of solvents phase
ratiot-butyl
methyl
ether
acetonitrile water
-5 10 0 10 45/55
-4 9 1 10 43/57
-3 8 2 10 41/59
-2 7 3 10 38/62
-1 6 4 10 36/64
0 5 5 10 34/66
+1 4 6 10 33/67
Solvent	System	Maps
QNEOI
Yb
MZAUFVRGCDXHTr
4:6:10
ZQNE
OIYb
UFMVARGCDrTXH
5:5:10
ZQNE
OIYb
UFMVARCDGrTXH
6:4:10
ZQNE
OIYb
UFMVARGCDrTXH
7:3:10
ZQNE
OIYb
UFMVARDGCrTXH
8:2:10
ZQNE
OIYb
UFMRVACDGrTXH
10:0:10
32
K <
16
K <
32
8
? KD <
16
4
K <
8
2
? KD <
4
1
? KD <
2
0.5
? KD <
1
0.25
? KD <
0.5
0.125
K <
0.25
0.0625
K <
0.125
0
KD <
0.0625
K
bins
QNEOI
Yb
MZAUFVRGCDXHTr
4:6:10
ZQNE
OIYb
UFMVARGCDrTXH
5:5:10
ZQNE
OIYb
UFMVARCDGrTXH
6:4:10
ZQNE
OIYb
UFMVARGCDrTXH
7:3:10
ZQNE
OIYb
UFMVARDG
ZQNE
OIYb
UFMRVA
32
Ki <
„
16
Ki <
32
8
Ki <
16
4
Ki <
8
2
Ki <
4
1
Ki <
2
0.5
Ki <
1
0.25
Ki <
0.5
0.125
Ki <
0.25
0.0625
ÂŁ Ki
0.125
0
ÂŁ Ki
0.0625
i
Sweet
Spot
terAcWat
SolventSystemMap
of GUESSmixstandards
ÂŁ ÂŁ ÂŁ ÂŁ ÂŁ ÂŁ ÂŁ ÂŁ ÂŁ
G
A
V
C
C
R
X
DN
COOHOH
HOOC
OH
OH
O
O
OH
OH
N
N N
N
O
O
CH3
CH3
H3C
OHO
HO
OH
HO
O
OH
N
H
N
O
H3CO OCH3
O
H3CO
OCH3
OCH3
OCH3
OH
OH
O
O
O
CH3
O OHO
OCH3
OH
OH
N
COOHOH
HOOC
OH
OH
O
O
OH
OH
N
N N
N
O
O
CH3
CH3
H3C
OHO
HO
OH
HO
O
OH
N
H
N
O
H3CO OCH3
O
H3CO
OCH3
OCH3
OCH3
OH
OH
O
O
O
CH3
O OHO
OCH3
OH
OH
HterAcWat
system #
relative proportions of solvents phase
ratiohexane tBME acetonitrile water
-8 10 0 10 0 40/60
-7 9 1 9 1 41/59
-6 8 2 8 2 41/59
-5 7 3 7 3 43/43/14
-4 7 3 6 4 45/24/31
-3 6 4 6 4 44/28/28
-2 7 3 5 5 47/10/43
-1 6 4 5 5 46/14/40
0 5 5 5 5 51/11/38
+1 4 6 5 5 63/37
+2 3 7 5 5 66/34
+3 4 6 4 6 58/42
+4 3 7 4 6 59/41
+5 3 7 3 7 55/45
+6 2 8 2 8 50/50
+7 1 9 1 9 49/51
+8 0 10 0 10 45/55
KD
intervals
0
≀ KD < 0.0625
0.0625
≀ KD <
0.125
0.125
≀ KD <
0.25
0.25
≀ KD <
0.5
0.5
≀ KD <
1
1
≀ KD <
2
2
≀ KD <
4
4
≀ KD <
8
8
≀ KD <
16
16
≀ KD <
32
32
≀ KD <
∞
10:0:10:0
rTXHGDC
RFVUAQN
EMZ
O I Y b
8:2:8:2
rTXHGDC
RFVUAQN
E MZ O I Yb
4:6:5:5 rTXH DCG RF AVU Q M ZN
E
OIYb
4:6:4:6 rTXH DCG RF AVU Q M ZN
E
OIYb
3:7:3:7 rTXH DC G RF
AV
U
M ZQ
NE
OIYb
2:8:2:8 rTXH DC G RA FVU M
ZQNE
OIYb
0:10:0:10 rTXH DCG RAV FUM
ZQNE
OIYb
Sweet Spot
HterAcWatSolvent System Map
Comparing SS in different families
r T X H C D G R V A F U M Z Q N E O I Y b
c) terAcWat6:4:10
polar r T X H D C G V A F U M N E R Z Q O I Y b nonpolar
a) EBuWat
r T X H C D G R F V A U Q M Z N E O I Y b
d) HterAcWat4:6:4:6
r T X H C D G R V A F U M Z Q N E O I Y b
b) terAcWat
Friesen	JB,	Pauli	GF.	Rational	development	of	solvent	system	families	in	counter-current	
chromatography.	J. Chromatogr.	A,	1151,	51-59,	2007;

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