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Improvement of the Fractional Precipitation Process for the Purification of (+)-Dihydromyricetin

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(1)

(+)-Dihydromyricetin 정제를 위한 분별침전공정 개선

임민경, 김진현*

공주대학교화학공학부

Received: December 10, 2013 / Revised: December 31, 2013 / Accepted: January 2, 2014

서 론

Hovenia dulcis

Ampelopsis grossedentata

유래생리활 성물질인

(+)-dihydromyricetin [(+)-ampelopsin] (Fig. 1)

알코올분해질환치료에효능이뛰어난기능성물질 숙취해소보호관련기능성식품의약품의원료로 사용되는 물질이다

[1, 6, 14, 16, 22]. Du

[4]

Ampelopsis grossedentata

유래

(+)-dihydromyricetin

고혈압억제에 상당히효과가있음을보고하였으며

Yoshikawa

[20]

에탄올에의한근육이완억제효과에탄올의체내 사촉진과보호효과등이있음을보고하였다

.

또한 러지효능이보고되기도하였다

[21].

생리활성물질인

(+)-dihydromyricetin

상업화

(

기능성 또는의약품

)

위해서는유용성분의대량분리정제 필수적이지만이에관한연구는아직까지상당히미흡한 실정이다

.

특히산업적대량생산에직접활용될있는

정제방법에대한연구는전무한실정이다

.

다만유기 용매를이용한추출크로마토그래피를이용한낮은순도

(<10%)

(+)-dihydromyricetin

얻거나테르페노이드

,

,

엽록소

,

페놀등이포함되어있는조추출물

(crude extract)

얻는것에제한적으로연구가진행되었다

[18, 24].

또한 고순도정제를위한공정으로고가의크로마토그래피를

용하고 있거나 처리없이 추출을 거친 조생성물

(crude

product)

high performance liquid chromatography (HPLC)

의해서바로최종정제하여경제적측면에서많은문제 있으며또한산업적대량생산을위한스케일업에많은

Improvement of the Fractional Precipitation Process for the Purification of (+)-Dihydromyricetin

Min-Kyoung Lim and Jin-Hyun Kim*

Department of Chemical Engineering, Kongju National University, Cheonan 330-717, Republic of Korea

Fractional precipitation is a simple method for purifying (+)-dihydromyricetin extracted from biomass. However, the fractional precipitation process has been inherently problematic due to the lengthy precipitation time that is required. The fractional pre- cipitation time was shortened and (+)-dihydromyricetin yield was improved by increasing the surface area per working volume (S/V) of the reacting solution through the addition of a cation exchange resin (Amberlite 200, Amberlite IR 120Na, Amberlite IR 120H, or Amberlite IRC 50). Most of the (+)-dihydromyricetin (>90%) could be obtained after about 16 h of fractional precipita- tion using Amberlite 200. Since high-purity (+)-dihydromyricetin can be obtained at a high yield and the precipitation time can be reduced by increasing the surface area available for precipitation, this improved method is expected to minimize solvent usage and the size and complexity of the high performance liquid chromatography operation required for (+)-dihydromyricetin purification.

Keywords: (+)-Dihydromyricetin, purification, fractional precipitation, surface area, improvement

*Corresponding author

Tel: +82-41-521-9361, Fax: +82-41-554-2640 E-mail: [email protected]

© 2014, The Korean Society for Microbiology and Biotechnology Fig. 1. The structure of (+)-dihydromyricetin.

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26 Lim et al.

어려움이따른다

[4].

2008

분별침전

(fractional precipitation)

의해높은

(>83.2%)

(+)-dihydromyricetin

얻을있는효율적 정제공정이개발되었다

.

그러나분별침전공정에서침전

많은시간

(~32 h)

소요되어대량생산공정에적용되는

여전히어려움이있다

[13].

따라서연구에서는분별침

전을위한반응기내부의반응액부피당표면적을증가시켜 분별침전에소요되는시간을획기적으로단축시킬있는 새로운방법을개발하고자하였다

.

이러한연구결과는기존 분별침전방법에의한

(+)-dihydromyricetin

정제공정의 문제점을개선함으로써

(+)-dihydromyricetin

대량생산에 매우유용하게활용될있을것으로판단된다

.

재료 및 방법

(+)-Dihydromyricetin 시료

연구에사용된

(+)-dihydromyricetin

Guilin Natural Ingredient, Inc. (Guilin, China)

에서 구입한 조추출물

(

순도

: 50.0%)

사용하였다

.

(+)-Dihydromyricetin 분석

(+)-Dihydromyricetin

분석을 위해

HPLC

시스템

(Waters, Milford, MA, USA)

이용하였다

.

분석은

C

18칼럼

(4.6

×

150 mm, 5

µ

m, Beckman, USA)

사용하였다

.

이동상은

gradient

조건으로

0.1%

트리플루오로아세트산

/

아세토니트릴

90/10 (v/v)

5

동안흘려준

30/70 (v/v)

전환하여

30

동안흘려주었다

.

유속은

1.0 ml/min,

시료주입량은

20

µ

l

이며

254 nm

에서

UV

의해검출하였다

. HPLC

분석은 정량곡선을이용하였으며

,

표준물질은

Guilin Natural Ingredient, Inc. (Guilin, China)

에서구입한순도

98%

품을사용하였다

[13].

분별침전(fractional precipitation)

조추출물의

(+)-dihydromyricetin

시료

(

순도

: 50.0%)

세톤에녹인

(0.1 g

조추출물

/1 ml

아세톤

),

증류수

(5 ml)

교반

(350 rpm)

하에방울씩떨어뜨려용해도차이를

용해

(+)-dihydromyricetin

침전을유도하였다

.

반응기부피

20 ml

이며반응액부피는

6 ml

이었다

.

반응액부피당 면적

(surface area/working volume, S/V)

조업이가능한 최대값

(0.428 mm

1

)

으로고정하여실험을수행하였다

. S/V

다음과같이계산하였다

.

S/V(mm

1

) = [

이온교환수지의표면적

(mm

2

)/

반응액부피

(mm

3

)] (1)

반응액부피당표면적을증가시키기위하여반응기내부

음이온교환수지

(Amberlite IRA 400OH, Amberlite IRA 400Cl, Amberlite IRA 910, Amberlite IRA 96, Amberlite IRA 67, Sigma-Aldrich, Seoul, Korea)

양이온교환수지

(Amberlite IR 120H, Amberlite IR 120Na, Amberlite 200, Amberlite IRC 50, Sigma-Aldrich)

각각 첨가하고 용액의

pH

9.0

조정한

4

o

C

에서 보관하여

(+)- dihydromyricetin

침전물을얻었다

.

실험에사용된이온교 환수지의입자크기는

16-50 mesh

이며표면적은구의표면 계산방법으로구하였다

.

이온교환수지는

35

o

C

에서하루 동안건조한실험에사용하였다

. (+)-Dihydromyricetin

분별침전 개략도를

Fig. 2

나타내었다

.

침전

(+)-

dihydromyricetin

침전물을 여과지

(150 mm, Whatman, Buckinghamshire, UK)

여과하여침전물을

35

o

C

에서

24

동안진공오븐

(UP-2000, EYELA, Japan)

에서건조하였

.

건조된침전물의순도와수율은

HPLC

분석하였다

.

침전물 형태 확인

분별침전공정에서

(+)-dihydromyricetin

침전물형태를 찰하기 위해 전자현미경

SV-35 Video Microscope

시스템

(Some Tech, Korea)

사용하였다

.

분별침전 동안

(+)- dihydromyricetin

침전물을고배율

(

×

100)

에서관찰하였다

.

관찰된

(+)-dihydromyricetin

침전물은

IT-Plus

시스템

(Some Tech, Korea)

에서동화상으로확인하였으며이를

(+)-dihydromyricetin

침전물의형태를확인하였다

[11].

결과 및 고찰

(+)-Dihydromyricetin 분별침전공정

분별침전은생리활성물질인

(+)-dihydromyricetin

효율 적으로정제할있는매우간편한방법으로

,

용해도차이 이용하여높은순도의

(+)-dihydromyricetin

고수율로

Fig. 2. Schematic diagram of fractional precipitation by

increasing surface area using ion exchange resin for the puri-

fication of (+)-dihydromyricetin.

(3)

얻을있는대표적인정제공정이다

[13].

기존문헌보고에 따르면

(+)-dihydromyricetin

분별침전을위한최적조건으 아세톤

/

증류수

,

초기

(+)-dihydromyricetin

농도

,

보관 온도

, pH

각각

1/5 (v/v), 0.1 g/ml, 4

o

C, 9.0

이었다

[13].

어진최적의분별침전조건으로실험을수행하여분별침전

동안 침전물을여과

,

건조

HPLC

분석을 수행한 결과

,

Fig. 3

에서보는바와같이분별침전

24

시간까지수율

(~70%)

급격히증가하다

24

시간이후거의변화가없었다

.

반면

별침전동안순도

(80-85%)

변화는미미함을있었다

.

이러한경향은기존에보고된연구결과

[13]

유사하였으

,

분별침전에많은시간

(24-32

시간

)

소요됨을확인할 있었다

.

반응액 부피당 표면적(S/V) 증가의 영향

분별침전은간단하고효율적으로정제할있는방법이 기는하지만분별침전에많은시간

(24-32

시간

)

소요되어

(+)-dihydromyricetin

대량생산에어려움이따른다

.

이러 분별침전에소요되는침전시간문제를개선하기 하여

,

반응기내부의 반응액부피당표면적이 증가된분별 침전공정을 도입하고자 하였다

.

분별침전공정에서

(+)- dihydromyricetin

침전되는양상을살펴결과

,

반응기 바닥과벽에얇게침전되어존재하는것을있었다

.

대부분의결정화는외부표면

(

외부불순물입자

,

반응기

,

교반장치표면

)

도움을받아핵이생성된다

[7-10].

이러한사실을토대로침전공정에서반응기내부의반응액

부피당표면적

(S/V)

증가시켜

(+)-dihydromyricetin

전할있는공간을증가시켜줌으로써침전효율을향상시 키고자하였다

.

기존문헌의분별침전을위한최적조건을 대로아세톤

/

증류수

,

보관온도

,

초기

(+)-dihydromyricetin

농도

, pH

각각

1/5 (v/v), 4

o

C, 0.1 g/ml, 9.0

고정하고

,

반응기내부의반응액부피당표면적

(S/V: 0.428 mm

1

)

가를위해양이온교환수지와음이온교환수지를각각첨가하 분별침전을수행하였다

. Fig. 4

에서보는바와같이침전 시간이경과함에따라

(+)-dihydromyricetin

수율도증가하 였다

.

반응기내부표면적을증가시키지않은경우에침전

24

시간경과수율은

70.0%

정도인반면표면적증가를

양이온교환수지강산성수지인

Amberlite IR 120H

첨가한 경우

83.0%, Amberlite IR 120Na

첨가한 경우

89.3%, Amberlite 200

첨가한경우

90.9%,

양이온교환수 약산성수지인

Amberlite IRC 50

첨가한 경우

75.0%

각각나타났다

.

표면적증가에의해침전효율이

향상됨을있었다

.

특히

Amberlite 200

경우침전

16

시간에높은수율

(>90%)

나타내어상대적으로짧은 전시간에높은수율로

(+)-dihydromyricetin

얻을있었

.

이러한결과는표면적증가물질과

(+)-dihydromyricetin

간의친화력차이때문으로판단된다

[5, 12].

반면표면적

가를 위한 음이온교환수지인

Amberlite IRA 400OH

Amberlite IRA 400Cl

경우에는적은양의침전물이형성 되었으나수율이매우낮았으며

Amberlite IRA 910, Amberlite IRA 96, Amberlite IRA 67

경우에는침전물이전혀형성

되지않았다

.

순도는

Fig. 5

에서보는바와같이침전시간이

경과할수록소폭증가하였으며

,

침전

24

시간에서의순도는 반응기내부표면적을증가시키지않은경우

80.0%,

표면적

Fig. 3. Effect of precipitation time on the purity and yield of

(+)-dihydromyricetin at a fixed acetone/distilled water ratio (1/5, v/v), precipitation temperature (4

o

C), pH (9.0), and initial concentration (0.1 g/ml) in fractional precipitation process .

Fig. 4. Effect of cation exchange resin used to increase sur-

face area per working volume (S/V: 0.428 mm

-1

) on the yield

of (+)-dihydromyricetin during fractional precipitation.

(4)

28 Lim et al.

증가를위해양이온교환수지강산성수지인

Amberlite IR 120H

첨가한경우

89.5%, Amberlite IR 120Na

첨가한 경우

90.0%, Amberlite 200

첨가한경우

90.2%,

양이온교 환수지약산성수지인

Amberlite IRC 50

첨가한경우

89.6%

각각나타났다

.

분별침전

24

시간에서표면적증가물

질로양이온교환수지인

Amberlite 200

첨가한경우가장 높은순도

(90.2%)

수율

(90.9%)

얻을있었다

.

음이온교환수지의경우표면적증가물질첨가에의한

응액부피당표면적

(S/V)

증가에도불구하고침전물이형성

되지 않는 이유를 조사하였다

.

음이온교환수지에

(+)- dihydromyricetin

흡착되었을가능성을확인하기위하여

,

분별침전

24

시간경과상등액

(supernatant)

에서의

(+)- dihydromyricetin

함량을분석하였다

. Table 1

에서보는 같이침전물이미량형성되었던

Amberlite IRA 400OH

Amberlite IRA 400Cl

경우상등액에서의

(+)-dihydromyricetin

함량은각각

31.3%

33.2%

이었다

.

반면전혀침전물이 성되지 않았던

Amberlite IRA 910, Amberlite IRA 96, Amberlite IRA 67

경우상등액에서의

(+)-dihydromyricetin

함량은각각

17.2%, 17.5%, 19.7%

이었으며침전물이미량 생성된

Amberlite IRA 400OH

Amberlite IRA 400Cl

상등액에서의

(+)-dihydromyricetin

함량이현저히낮음 확인할있었다

.

,

음이온교환수지

Amberlite IRA 910, Amberlite IRA 96, Amberlite IRA 67

경우

Amberlite IRA 400OH

Amberlite IRA 400Cl

보다많이이온교환 수지에흡착됨을있었다

.

이러한결과로부터표면적증 가물질로음이온교환수지를사용한분별침전의경우

,

침전 물이원활하게형성되지않는이유는이온교환수지에대부분

(+)-dihydromyricetin

흡착되기때문으로판단된다

[17].

표면적 증가에 따른 (+)-dihyromyricetin 침전물 형태 변화

분별침전에서반응액부피당표면적

(S/V)

증가에따른 전물형태변화를조사하기위하여전자현미경을이용하여

(+)-dihydromyricetin

침전물을확인하였다

.

양이온교환수지 음이온교환수지에서의침전양상을

Fig. 6

Fig. 7

나타내었다

.

표면적증가물질종류와침전시간에따라 양상이달라짐을있었다

.

동일한침전시간에서는 표면적증가물질을첨가하지않은경우에비해표면적증가 물질인양이온교환수지

(Amberlite IR 120H, Amberlite IR 120Na, Amberlite 200 Amberlite IRC 50)

음이온교환수

(Amberlite IRA 400OH, Amberlite IRA 400Cl)

첨가 경우

(+)-dihydromyricetin

침전물의크기가작아짐을 있었다

.

표면적증가물질을첨가하지않은경우에비해 면적증가물질인이온교환수지를첨가한경우결정성장을

저해받았기때문으로판단된다

[11].

또한표면적증가물질의

종류에따라입자형태와크기가다른이유는표면적증가물 질의친화력

(affinity)

차이때문으로판단된다

[5, 12].

,

면적증가물질과

(+)-dihydromyricetin

입자의친화력이증가 할수록

(+)-dihydromyricetin

입자성장을저해하는효과 적인공간적저해요소

(steric barrier)

역할을하기때문에 전물의크기가감소하게된다

.

이러한현상은원료의약품인

megestrol acetate [2], spironolactone [3], atorvastatin calcium [23]

에서도확인되었는데

,

침전공정에서고분자물질을첨가 하여성공적으로이들원료의약품의입자크기를효과적으로 절할있었다

.

일반적으로원료의약품

(active pharmaceutical ingredient, API)

경우입자크기를작게하여활용도 높이고자한다

.

입자크기가작아질수록제형용해

(dissolution rate),

약물 분산의 균일성

(uniformity of drug dispersion),

경구생체이용률

(oral bioavailability)

향상시킬있는장점을가지고있기때문이다

[2, 11, 19].

Fig. 5. Effect of cation exchange resin used to increase sur- face area per working volume (S/V: 0.428 mm

−1

) on the purity of (+)-dihydromyricetin during fractional precipitation.

Table 1. Distribution of (+)-dihydromyricetin in supernatant of precipitator after fractional precipitation (24 h) at different anion exchange resins used to increase surface area per working volume (S/V: 0.428 mm

−1

).

Ion exchange resin Distribution of (+)-dihydromyricetin in supernatant (%)*

Amberlite IRA 400OH 31.3 ± 2.0

Amberlite IRA 400Cl 33.2 ± 2.2

Amberlite IRA 910 17.2 ± 1.4

Amberlite IRA 96 17.5 ± 1.6

Amberlite IRA 67 19.7 ± 1.7

*Data are shown as distribution (%) ± SD.

(5)

또한입자크기가작을수록정제건조단계에서잔류수

잔류용매제거에도상당히도움이되기때문이다

[15].

이러한이유로연구결과인표면적증가물질인이온교환 수지를첨가에의한

(+)-dihydromyricetin

입자크기감소는 의약품의활용측면에서도유용하게사용될있을것으로 판단된다

.

요 약

연구에서는 바이오매스 유래 생리활성물질인

(+)-

dihydromyricetin

효율적으로정제하기위하여

,

반응액

피당표면적

(S/V)

증가된새로운개념의분별침전공정을

도입하였다

.

분별침전

24

시간에서반응기내부표면적을

가시키지않은경우순도와수율은각각

80.0%

70.0%

반면표면적증가를위해양이온교환수지인

Amberlite 200

첨가한경우순도와수율은각각

90.2%

90.9%

가장 효과적인표면적증가물질임을있었다

.

특히

Amberlite

200

경우상대적으로짧은침전시간

(16

시간

)

높은수율

(>90%)

(+)-dihydromyricetin

얻을있어침전에소요 되는시간을효과적으로단축시킬있었다

.

동일한침전시

Fig. 6. Optical images of (+)-dihydromyricetin precipitate formed by fractional precipitation at 8 h, 16 h, 24 h: control (A); cation

exchange resins Amberlite 200 (B); Amberlite IR 120H (C); Amberlite IR 120Na (D); Amberlite IRC 50 (E). Scale bar indicates

500 µm.

(6)

30 Lim et al.

간에서는표면적증가물질을첨가하지않은경우에비해 면적증가물질을첨가한경우침전물의입자크기가감소함 있었다

.

이러한연구결과는기존의분별침전방법 의한

(+)-dihydromyricetin

정제공정의문제점을개선함 으로써

(+)-dihydromyricetin

대량생산에매우유용하게 용될있을것으로판단된다

.

References

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Sci. 7: 263-268.

Fig. 7. Optical images of (+)-dihydromyricetin precipitate formed by fractional precipitation at 8 h, 16 h, 24 h: anion exchange resins Amberlite IRA 400OH (A); Amberlite IRA 400Cl (B); Amberlite IRA 910 (C); Amberlite IRA 96 (D); Amberlite IRA 67 (E).

Scale bar indicates 500 µm.

(7)

2. Cho EB, Cho WK, Cha KH, Park JS. 2010. Enhanced dissolu- tion of megestrol acetate microcrystals prepared by antisol- vent precipitation process using hydrophilic additives. Int. J.

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8. Kang I, Kim JH. 2012. Effect of reactor type on the purification efficiency of paclitaxel in the increased surface area fractional precipitation process. Sep. Puri. Technol. 99: 14-19.

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Biotechnol. Bioproc. Eng. 13: 274-278.

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112-116.

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Porcelain ampelopsis. CN Patent 1,393,443.

수치

Fig. 4. Effect of cation exchange resin used to increase sur- sur-face area per working volume (S/V: 0.428 mm -1 ) on the yield of (+)-dihydromyricetin during fractional precipitation.
Fig. 5. Effect of cation exchange resin used to increase sur- sur-face area per working volume (S/V: 0.428 mm −1 ) on the purity of (+)-dihydromyricetin during fractional precipitation
Fig. 7. Optical images of (+)-dihydromyricetin precipitate formed by fractional precipitation at 8 h, 16 h, 24 h: anion exchange resins Amberlite IRA 400OH (A); Amberlite IRA 400Cl (B); Amberlite IRA 910 (C); Amberlite IRA 96 (D); Amberlite IRA 67 (E).

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