Field of the invention
[0001] The present invention relates to method for extracting total salvianolic acid from
Danshen.
Background of the invention
[0002] Danshen, also known by its botanical name
Radix Salvia Miltiorrhizae, is one of the most common-used traditional Chinese medicines (TCM) in China. It mainly
consists of two categories of chemical ingredients, namely the water-soluble and the
non water-soluble. Dating back to the early 20
th century, the chief research on these ingredients has always been concentrated on
the non water-soluble ones represented by tashinone, and achieved great success after
decades of efforts. It is not until the beginning of 1980s that, after a lot of work,
our scientists have studied Danshen's water-soluble ingredients, and first reported
structure of the water-soluble one, Danshensu. Afterward, tens of water-soluble ones
have also been discovered one after another with the definitive chemical structure.
Subsequently it has been proven that, of the active ingredients in Danshen's water-soluble
ones, the most effective is phenolic acid compounds, such as salvianoic acid A(1),
B(2), C(3), D(4), E(5), F(8), G(9), H(11), I(12), J(13), rosmarinci acid (6), alkannic
acid (7), isosalvianoic acid C(10), glucoside of rosmarinci acid(14), etc. (
Lian-Niang Li, J. Chinese Pharmaceutical Sciences 1997, 6, 57-64). Pharmacologically, a variety of activities of these salvianolic acid compounds
have already been reported. For example, Salvianolic acid A has significant protecting
effects on cardiac muscle cell caused by ischemic reperfusion (I/R), and totalphenolic
acid has strong anti-arrhythmia effect induced by I/R; Salvianolic acid A, B and totalphenolic
acid have showed markedly protective effects against brain damage caused by I/R in
rats by lowering content of MDA in brain tissues; there are plenty more other effects
for the salvianolic acid as follows: anti-thrombus effects, protective effect on liver
and kidney, anti-oxidation and inhibiting lipid super oxidation, as well scavenging
puperoxide anion and free radical etc. (
Du Guanhua etal, Basic medical science and clinics, 2000, 20 (5): 10-14).
[0003] At present, a great number of processes of extracting Salviamolic acid have been
reported, but most of them are mainly focused on passing resin column following extracting
by water. For example, Takashi Tanaka et al revealed the method of extracting salvainolate
(
Chemical Pharmaceutical Bulletin, 1989, 37 (2),340~344). Besides, there have also been many other scientists who have adopted similar methods
for extracting phenolic compounds from Danshen, such as
Koji Hase et al (Planta Medica, 1997, 63, 22~26), Xu Yaming et al (China patent
CN1247855A, published in March, 2000), Liu Ping et al (China patent
CN1270809A, published in October, 2000), and Li Lianniang (China Patent Application No.
0114228.2, filed on September 2001). But all of above-mentioned processes for extracting have a common problem in industrialization,
namely a great deal of water need to be concentrated. Because of the instability,
the concentrating temperature of total salvainolic acid water decoction must be varying
between 50°C and 60°C, which accordingly will result in both the difficulties in techniques
and rise in cost. Meanwhile, the lasting heating process, although between 50°C and
60°C, will also produce a series of serious problems including instability, and therefore
affect its quality and curative effect. Finally, all these problems make it almost
impossible for the industrialization. Another shortcoming of these already-existing
processes is that the low yield, generally between 2% and 3%, limits its application
in the industry.
Summary of the invention
[0004] Accordingly, one object of the present invention is, obviating the drawbacks of the
prior art, to provide a method for preparation of totalphenolic acid from Danshen
with high yield, low cost, good quality, and convenience of being applied in the industry.
Thus, the present inventions provides a method for the preparation of total salvianolic
acid according to appended Claim 1.
Detailed description of the preferred embodiments
[0005] The present invention of preparing totalphenolic acid mainly consists of the following
steps, namely decocting Danshen with hot water; separating the decoction with Polyamide
column and macroporous adsorption resin.
[0006] The totalphenolic acid may be obtained by the following scheme:
- (a) After the impurities is eliminated, the Danshen is cut into little sections or
pulverized into crude powder, and decocted with hot water. The decoction is filtered
after its pH value being adjusted to acidity.
- (b) Applying said decoction on a polyamide column, and washing the column with water
to neutral condition. Eluting the column with weak basic aqueous solution, and collecting
the eluent.
- (c) Applying the eluent on the macroporous adsorption resin column, after acidifying
the basic eluent of step (b). At first, washing the column with water to neutral condition,
and then eluting the column with hydrous or anhydrous lower alcohol. Afterward, collecting
the eluent.
- (d) Concentrating the eluent under reduced pressure until there is no ethanol, and
drying it to obtain the total salvianolic acid.
[0007] In step (a), Danshen is extracted with hot water for 2 to 4 times, 0.5 to 2h each,
and the extracting temperature is 60 to 100°C, preferably 90 to 100°C; the extract
solution after each extracting process, alone or combined, preferably combined, is
further treated; the pH value is adjusted with acid to less than 4 , preferably below
2.
[0008] In step (b), the concentration of weak basic aqueous solution preferably is from
0.01% to 2%, most preferably 0.08% to 0.5%, and the common polyamide materials is
used, for example, polycaprolactam (nylon-6).
[0009] In step (c), the common macroporous adsorbent resin is used, for example styrene-type
adsorbent resin; the pH value of weak basic fractions are adjusted by acid to below
4, preferably below 2; the number of carbon atoms in lower alcohol ranges from 1 to
5, for example, the methanol, ethanol, etc.; the eluting concentration is 40% to 95%,
preferably 60% to 95%. However, in view of the safety in large-scale industrialized
production, lowering cost and process simplification, eluting by 95% ethanol is the
best option to achieve satisfying purpose.
[0010] In step (d), if necessary, said concentrate is dried, such as by lyophilization,
following being filtered with microporous filter membrane.
[0011] The totalphenolic acid produced by the method of this invention can be formulated
into any kind of pharmaceutically acceptable dosage form, and can also be combined
with other medicaments or active ingredients.
[0012] Compared with the prior art, this invention has the following advantages:
- 1. Easiness of industrialization. In the prior art, a great deal of water need to
be concentrated during the process, resulting in the difficulties in industrialization.
Such a defect is overcome in the present invention, wherein, without heating and decompression,
lot of water are surprisingly removed. Consequently, the processes and conditions
are optimized with no energy consuming and environment pollution. So, with the advantages
in respect of techniques or environmental protection, it is easy to bring about industrialization.
- 2. Reduction of loss in active ingredients. The present invention can effectively
avoid a loss of active ingredients caused by precipitation with alcohol in prior art,
and also prevent instability of totalphenolic acid in concentrating a lot of water.
All these above would in effect avoid the losses and decomposition of the active ingredients
during the process, so as to assure the stability of final product.
- 3. High yield. The yield of the products produced in the prior art (i.e. the dried
totalphenolic acid powder) is only 2%-3% by weight based on the crude herbal medicine;
while using the method of present invention, the yield is more than 4%, apparently
better than that of the prior art. Moreover, the content of totalphenolic acid in
the high quality final product is more than 80% with less impurity.
- 4. Lower cost. In the method of present invention, a great deal of water can be concentrated
and removed without heating and decompression, effectively reducing the energy consumption
and cost. In addition, the yield of the total phonelic acid by this invention is higher,
and moreover its content in the final product is close to or higher than that of the
prior art, that is to say, more products with equal or better quality will be produced
from the same amount of crude herbal medicine. The lower cost will benefit a lot,
not only in the industrialization, but also the patients' economic interests, accordingly
bringing about a great social benefit.
- 5. The studies on animals also show the good effects of the totalphenolic acid produced
by the method of present invention.
Protective effect of the totalphenolic acid against cerebral artery ischemia in rats
1. Materials and Methods
[0013]
- 1) Animals: Male Wister rats, weighing from 200 to 220g (Certificate No. SCXK(Beijing)
2002-003), are obtained from the Animal Center of Beijing Medical University.
- 2) Reagents : Chloral Hydrate purchased from Shenyang reagent factory, Liaoning, China,
the batch number being 920401.
Red tetrazoline (TTC) from Beijing chemical plant, the batch number being 810911.
- 3) Apparatus: High-frequency electric knife purchased from Beijing medical electronic
apparatus factory.
The SXP-1B operating microscope from Shanghai medical optical instrument factory.
- 4) Tested agents: The total phenolic acid produced by Tianjin Tasly Modern TCM institute
according to the method of the present invention; and
The total salvianolic acid produced by Institute of Materia Medica, Chinese Academy
of Medical Sciences in accordance with the method of China Patent Application No.
01142288.2 filed on September, 2001.
Xiangdan injection, as control drug, purchased from Ya an Sanjiu pharmaceutical Co.
ltd, the bath number being 010901.
- 5) Formulation method of the tested agents and route of administration: The totalphenolic
acid and Xiangdan injection are diluted into desired concentration with sterilized
physiological saline, 10mg/kg and 20mg/kg for the totalphenolic acid, and 1 ml/kg
(equal to 1g/kg) for Xiangdan injection. By sublingual vein, both of these kinds of
drugs are administered 30 minutes after ischemia.
- 6) Groups: All rats are randomly divided into the following groups: sham operation
control group, ischemic control group, total phenolic acid ( Institute of Materia
Medica) 10mg/kg and 20mg/kg groups, total phenolic acid (Tasly) 1 0mg/kg and 20mg/kg
groups .
2. Method
[0014]
- 1) cerebral artery blockade (electric coagulation) ischemia in rats: Rats are anesthetized
by intraperitoneal injection of Trichloracetic aldehyde, 350mg/kg body weight, and
fixed on a board in a left lateral position. Under the operating microscope, the skin
is incised open via midline between the external auditory meatus and the canthus.
The zygomatic orthopedics is exposed, and removed thoroughly with orthopedics rongeur.
The fascia is nipped off along skull, and tempora fossa is exposed. Between the squamous
orthopedics and mandible is gently propped up with retractor, and at the bottom of
the skull the skull window is opened so as to uncover cerebral middle artery. The
middle artery is burnt out with the high-frequency electric knife in order to block
the blood flow, forming a model of cerebral local ischemia. After 30 minutes, the
rats are administrated through sublingual vein, and sent back to cage for feed. The
room temperature is rigorously kept between 24°C and 25°C.
- 2) The measurement of cerebral infarct volume: 24 hours after the cerebral middle
artery is blocked, the rats are beheaded and their cerebrums are taken out. The whole
cerebrum is kept at 4°C in a beaker filled with normal-saline in a refrigerator for
10 minutes, and then the olfactory bulb, the cerebellum and the low-set brain stem
are removed. Along the coronal plane, the cerebrum is chipped into 5 slices, and put
into 5 ml dyeing solutions containing 1.5 ml of 4% TTC and 0.1 ml of 1 mol/L di-potassium
hydrogen phosphate, light-proof incubated in water bath 37°C for 30 minutes. The slices
of cerebrum are taken out and put into 10% formalin for solidification. As a result,
the normal cerebral tissue is rose pink, and the ischemic one is white. The weight
planimetry is used to measure the area of infarct, and further the percentage of the
area of infarct to the whole cerebrum hemisphere is calculated.
- 3) The measurement of content of water in the cerebrum: 24 hours after blockade of
the cerebral middle artery, the rats are executed, and the whole cerebrum is gently
taken out. After that the olfactory bulb, the cerebellum and the low-set brain stem
are taken away, the cerebrum is weighed (regarded as the cerebral wet weight). After
that, the cerebrum is dried in an oven at 105°C till that the weight is constant (about
48 hours), and is weighed again (referred to as the cerebral dry weight). The final
content of water in the cerebrum is calculated with the following formula:

3. Result
[0015] Protective effect of the totalphenolic acid against the cerebral middle artery coagulation
ischemia in rats
| group |
dosage
mg / kg |
number of animal
N |
Volume of infarct (%) |
the content of water ( %) |
| sham operation control group |
|
12 |
0 |
79.4586t0.3402** |
| ischemic control group |
|
10 |
7.0194±4.389 |
80.4487±0.8614 |
| Xiangdan injection |
1m//kg |
12 |
0.7553±2.2188** |
79.43644±0.5061 |
| total phenolic acid (Institute of Materia Medica) |
10 |
12 |
3.2919±3.205# |
79.4723±0.5475** |
| total phenolic acid (Institute of Materia Medica) |
20 |
12 |
1.5156±2.7602* |
79.4806±0.6819* |
| total phenolic acid (Tasly) |
10 |
10 |
2.8170±3.2621# |
79.4529±0.7693* |
| total phenolic acid (Tasly) |
20 |
10 |
1.5328±3.2575* |
79.5914±0.5843* |
note: (1) **P<0.01,*P<0.05, two-sided test, comparing with ischemic control group.
#P<0.05, one-sided test, compared with ischemic control group.
(2) 1ml/kg the Xiang dan injection as a control is equal to 1g/kg of crude herbal
medicine;
10mg/kg totalphenolic acid (Tasly) is equal to 0.25g/kg of crude herbal medicine (calculated
with yield being 4%); and
20mg/kg totalphenolic acid (Tasly) is equal to 0.5g/kg of crude herbal medicine (calculated
with yield being 4%). |
4. Conclusion
[0016] By using the method of coagulation in middle cerebral artery to attain cerebral ischemia
in rats, the protective effect of the totalphenolic acid produced respectively by
Tasly and Institute of Materia Medica on cerebral artery ischemic has been observed.
The result revealed that, 30 min after administration in vein, 10mg/kg and 20mg/kg
of both two kinds of phenolic acids could markedly alleviate cerebral edema and cerebral
infarction caused by ischemia. Moreover, the said two kinds of phenolic acids had
the same effect administered in the same dosage. All above studies have showed that
two phenolic acids had the same effect of anti-cerebral ischemia.
[0017] The totalphenolic acid obtained according to this invention can be formulated into
pharmaceutically acceptable dosage forms, including tablet, capsule, granules, oral
liquid, sustained-release formulation, control-release formulation, gel, ointment,
salve, cream, suppository, injection, powder, patch, dripping pill and suspension.
[0018] The totalphenolic acid can be used for the treatment of diseases, including cardiovascular
and cerebrovascular disease, nephrosis, hepatopathy, pneumonia, pneumocardial disease,
pancreatitis, diabetes mellitus, cervical syndrome, ocular fundus vascular disease,
ocular fundus neuro-disease, migrain, chronic gastritis, dizziness, orthopedics disease,
mountain sickness and senile dementia.
Embodiments
[0019] The following examples are offered for purposes of illustration only and are not
intended to limit the scope of the invention in any way.
Comparative Example
[0021] 5 Kg of Danshen herb is ground into crude powder, and is extracted at 100°C for three
times with deionized water added, specifically, extracted for 1 hour with 30L water
added the first time, and extracted for 0.5 hour with 15L water added the second and
third times respectively. The extract is concentrated to 5L at 50°C under reduced
pressure and cooled. Into the concentrate 14L of 95% ethanol is added. The mixture
is allowed to stand over night and filtered. Under reduced pressure, the ethanol is
recovered at 50°C. The obtained concentrate is applied on RA macroporous adsorption
resin (mainly containing styrene and chrysophenine , and the weight of dried resin
is 2kg). The resin is washed with deionized water until that the eluent had no apparent
α-naphthol reaction, and then eluted with 50% ethanol until that the eluent had no
obvious phenolic hydroxyl reaction with iron sesquichloride potassium ferricyanide
added. The fractions are concentrated at 50°C under reduced pressure. The mixture
is allowed to stand over night in a refrigerator, and filtered to produce the extract
of Total salvianolic acid. The pH of the said extract is adjusted with 2% sodium hydroxid
to 6.5, and the extract is freeze dried to produce 114g of totalphenolic acid. The
yield of the final product in crude drug is 2.3%. The analysis showed that the content
of totalphenolic acid in final product amounted to 83.72%, and Salvianolic acid B
was in amount of 54.41%.
[0022] Total salvianolic acid and Salvianolic acid B are analyzed according to the method
of Chinese Patent Application No.
01142288.3 filed on Sep. 2001.
- (1) Salvianolic acid B: analyzed by HPLC at 288 nm. The Salvianolic acid B CRS is
manufactured by Modem TCM Institute under Tianjin Tasly Group with purity of 98.0%.
- (2) Total salvianolic acid: Content= F (A-B) + B
wherein, A is the content of Total salvianolic acid calculated with the Salvianolic
acid B as CRS by ultraviolet spectrophotometry;
B is the content of Salvianolic acid B by HPLC;
F is correction factor 0.626.
EXAMPLE 1
[0023] 5 kg of Danshen herb is ground into crude powder, and is extracted at 100°C at the
state of lightly boiling for three times with deionized water, specifically, extracted
for 1 hour with water (x5.5 fold) added the first time, and extracted for 0.5 hour
with water (x3 fold) added the second and third times respectively. The extract is
combined, and the pH thereof is adjusted with 10% hydrochloric acid to 2.0. The extract
is filtered, and the filtrate is loaded on polyamide column (the amount of the dry
resin is two-thirds of that of the crude herb). The column is washed with deionized
water (x5 fold), and the washing is discarded. Then the column is eluted with 5 column
volumes of the 0.1% aqueous solution of sodium bicarbonate. The fraction was collected,
adjusted with 10% hydrochloric acid to pH 2.0, and is loaded on D
10, macro-porous resin column. The column is washed with deionized water to neutral
condition and the washing is discarded. Then the column is eluted with 95% ethanol,
and the colored belt is collected when it is eluted down. The fractions are concentrated
under reduced pressure to entire dryness. The above concentrate is dissolved with
water. The mixture is allowed to stand over night in refrigerator, and filtered by
0.3 µm mixed cellulose microporous membrane to produce extraction solution of Total
salvianolic acid. Immediately after this totalphenolic acid is adjusted with 2% sodium
hydroxide to pH 6.0, it is freeze dried to produce 221g of freeze-dried powders of
Total salvianolic acid. The yield of the final product is 4.4% based on the amount
of the crude herb. The analysis according to the method of Chinese Patent Application
No.
01142288.2 filed on Sep. 2001 shows that, the totalphenolic acid amounts to 83.94%, and Salvianolic acid B is 53.73%
in the final product.
Example 2
[0024] 5 kg of Danshen herb is ground into crude powder, and is extracted at 80°C for three
times with deionized water, specifically, extracted for 2 hours with water (×5.5 fold)
added the first time, and extracted for 1 hour with water (×3 fold) added the second
and third times respectively. The extracts are combined, and the pH thereof is adjusted
with 5% sulfuric acid to 1. The extract is filtered, and the filtrate is loaded on
polyamide column (the amount of the dry resin is two-thirds of that of the crude herb).
The column is washed with deionized water (x5 fold), and the washing is discarded.
Then the column is eluted with 4 column volumes of the 0.2% aqueous solution of sodium
bicarbonate. The fractions are collected, adjusted with 5% sulfuric acid to a pH of
1, and is loaded on AB-8 macro-porous adsorption resin column. The column is washed
with deionized water to neutral condition and the washing is discarded. Then the column
is eluted with 60% ethanol, and the colored belt is collected when it is eluted down.
The fractions are concentrated under the reduced pressure until it had no smell of
ethanol. The mixture is allowed to stand over night in refrigerator, and filtered
by 0.3 µm mixed cellulose micro-porous membrane to produce extraction solution of
Total salvianolic acid. Immediately after this totalphenolic acid is adjusted with
2% sodium hydroxide to pH 6.0, it is freeze dried to produce 227g of freeze-dried
powders of Total salvianolic acid. The yield of the final product is 4.5% based on
the amount of the crude herb. The analysis according to the method of Chinese Patent
Application No.
01142288.2 filed on Sep. 2001 shows that, the totalphenolic acid amounts to 83.15%, and Salvianolic acid B is 54.03%
in the final product.
EXAMPLE 3
[0025] 5 kg of Danshen herb is ground into crude powder, and is extracted at 100°C at the
state of lightly boiling for three times with deionized water, specifically, extracted
for 1 hour with water (×5.5 fold) added the first time, and extracted for 0.5 hour
with water (×3 fold) added the second and third times respectively. The extract is
combined, and the pH thereof is adjusted with 10% hydrochloric acid to 2.0. The extract
is filtered, and the filtrate is loaded on polyamide column (the amount of the dry
resin is two-thirds of that of the crude herb). The column is washed with deionized
water (x5 fold), and the washing is discarded. Then the column is eluted with 5 column
volumes of the 0.1% aqueous solution of sodium bicarbonate. The fractions are collected,
adjusted with 10% hydrochloric acid to a pH of 2.0, and is loaded on RA macro-porous
resin column. The column is washed with deionized water to neutral condition and the
washing is discarded. Then the column is eluted with 60% Methanol, and the colored
belt is collected when it is eluted down. The fractions are concentrated under the
reduced pressure until it had no smell of ethanol. The mixture is allowed to stand
over night in refrigerator, and filter by 0.3 µm mixed cellulose micro-porous membrane
to produce extraction solution of Total salvianolic acid. Immediately after this totalphenolic
acid is adjusted with 2% sodium hydroxide to pH 6.0, it is freeze dried to produce
224g of freeze-dried powders of Total salvianolic acid. The yield of the final product
is 4.5% based on the amount of the crude herb. The analysis according to the method
of Chinese Patent Application No.
01142288.2 filed on Sep. 2001 shows that, the totalphenolic acid amounts to 84.02%, and Salvianolic acid B is 54.17%
in the final product.
EXAMPLE 4
Formula of Total salvianolic acid capsule
[0026]
| Total salvianolic acid |
240g |
| Microcrystalline cellulose |
40g |
| Talcum powder |
1.4% |
| 3% ethanol solution of polyvidone |
appropriate |
| 1000 capsules are produced. |
|
[0027] Total salvianolic acid and microcrystalline cellulose are mixed thoroughly. 3% ethanol
solution of polyvidone is added into the mixture to make soft stuff. It is sifted
through 18-mesh screen sieve to give granules, and dried at 60°C for 30 to 45 min.
Then, talcum powder is added, and the mixture is stirred and filled into No. 1 capsule
shell to produce capsules each of which contains 240mg.
EXAMPLE 5
Formula of of Total salvianolic acid tablet
[0028]
| Total salvianolic acid |
240g |
| Microcrystalline cellulose |
40g |
| Talcum powder |
1.4% |
| 3% ethanol solution of polyvidone |
appropriate |
| 1000 tablets are produced. |
|
[0029] Total salvianolic acid and microcrystalline cellulose are mixed thoroughly. 3% ethanol
solution of polyvidone is added into the mixture to make soft stuff. It is sifted
through 18-mesh screen sieve to give granules, and dried at 60°C for 30 to 45 min.
Then, talcum powders are added, and the mixture is stirred and tableted.
EXAMPLE 6
Formula of Total salvianolic acid granula
[0030]
| Total salvianolic acid |
240g |
| Microcrystalline cellulose |
40g |
| Talcum powder |
1.4% |
| 3% ethanol solution of polyvidone |
appropriate |
| 500 sachets are produced. |
|
[0031] Total salvianolic acid and microcrystalline cellulose are mixed thoroughly. 3% ethanol
solution of polyvidone is added into the mixture to make soft stuff. It is sifted
through 18-mesh screen sieve to give granules, and dried at 60°C for 30 to 45 min,
and filled into sachets.
EXAMPLE 7
Formula of Total salvianolic acid powder for injection
[0032]
| Total salvianolic acid |
100g |
| Mannite |
30g |
| Antallin |
5g |
| Distilled water |
5ml |
[0033] The above ingredients are mixed well, lyophilized, and filled into 1000 vials.
1. A method for the preparation of total salvianolic acid comprising the steps of:
a. Extracting Danshen with water and acidifying the extract and filtrating;
b. Applying said Danshen extract on a polyamide column, washing the column with water
to neutral condition, discarding the washings, eluting the polyamide column with weak
basic aqueous solution, and collecting the fractions;
c. Applying the basic fractions of step (b) on a macroporous adsorption resin column
of styrene type, after acidifying the fractions, firstly washing the column with water
to neutral condition, discarding the washings, and then eluting the column with hydrous
or anhydrous lower alcohol; the eluent being collected, concentrated under reduced
pressure until no alcohol, and dried.
2. The method as recited in claim 1, wherein the heating extraction in step (a) by water
is repeated for 2-4 times, and for 0.5~2h each.
3. The method as recited in claim 1, wherein the temperature for the said extraction
of step (a) by water is 60~100°C.
4. The method as recited in claim 1, wherein the temperature for the said extraction
of step (a) by water is 90~100°C.
5. The method as recited in claim 1, wherein the said extract of step (a) is adjusted
with an acid to a pH value of below 4, and the basic fractions of step (c) is acidified
with an acid to a pH value of below 4.
6. The method as recited in claim 1, wherein the said extract of step (a) is acidified
with an acid to a pH value of below 2, and the basic fractions of step (c) is acidified
with hydrochloric acid or sulfuric acid to a pH value of below 2.
7. The method as recited in claim 1, wherein in step (b) 0.01~2% of aqueous weak basic
solution is used as eluant.
8. The method as recited in claim 1, wherein in step (b) 0.08~0.5% of aqueous solution
of sodium hydrogen carbonate is used as eluant.
9. The method as recited in claim 1, wherein the hydrous or anhydrous lower C1~C5 alcohol is used as the eluant in the step (c).
10. The method as recited in claim 1, wherein in the step (c) the column is eluted with
aqueous ethanol with a concentration of 40~95%.
11. The method as recited in claim 9 or 10, wherein the concentration of the lower C1~C5 alcohol or the aqueous ethanol is 60~95%.
12. The method as recited in claim 10, wherein the concentration of the aqueous ethanol
is 95%.
1. Verfahren zum Herstellen von Gesamt-Salvianolsäure, umfassend die Schritte
a) Extrahieren von Danshen mit Wasser und Ansäuern des Extrakts und Filtrierens;
(b) Aufbringen des Danshen-Extrakts auf eine Polyamidsäule, Waschen der Säule mit
Wasser bis zum neutralen Zustand, Wegwerfen der Waschlösungen, Eluieren der Polyamidsäule
mit schwacher, basischer, wässriger Lösung und Auffangen der Fraktionen;
(c) Aufbringen der basischen Fraktionen aus Schritt (b) auf eine makroporöse Adsorptionsharzsäule
des Styroltyps, nach Ansäuern der Fraktionen zuerst Waschen der Säule mit Wasser bis
zum neutralen zustand, Wegwerfen der Waschlösungen und dann Eluieren der Säule mit
wässrigem oder wasserfreiem niederem Alkohol, wobei das Elutionsmittel aufgefangen,
unter reduziertem Druck bis kein Alkohol vorhanden ist konzentriert, und getrocknet
wird.
2. Verfahren nach Anspruch 1, wobei die Erhitzungsextraktion in Schritt (a) durch Wasser
2 - 4-mal und jeweils 0,5 - 2 h lang wiederholt wird.
3. Verfahren nach Anspruch 1, wobei die Temperatur für die Extraktion des Schritts (a)
durch Wasser 60 - 100 °C beträgt.
4. Verfahren nach Anspruch 1, wobei die Temperatur für die Extraktion des Schritts (a)
durch Wasser 90 - 100 °C beträgt.
5. Verfahren nach Anspruch 1, wobei der Extrakt aus Schritt (a) mit einer Säure auf einen
pH-Wert unter 4 eingestellt wird und die basischen Fraktionen des Schritts (c) mit
einer Säure auf einen pH-Wert unter 4 eingestellt werden.
6. Verfahren nach Anspruch 1, wobei der Extrakt aus Schritt (a) mit einer Säure auf einen
pH-Wert unter 2 angesäuert wird und die basischen Fraktionen des Schritts (c) mit
Salzsäure oder Schwefelsäure auf einen pH-Wert unter 2 angesäuert werden.
7. Verfahren nach Anspruch 1, wobei in Schritt (b) 0,01 - 2 % wässrige, schwache, basische
Lösung als Elutionsmittel verwendet wird.
8. Verfahren nach Anspruch 1, wobei in Schritt (b) 0,08 - 0,5 % wässrige Lösung von Natriumhydrogencarbonat
als Elutionsmittel verwendet wird.
9. Verfahren nach Anspruch 1, wobei der wässrige oder wasserfreie niedere C1- ~ C5-Alkohol in Schritt (c) als Elutionsmittel verwendet wird.
10. Verfahren nach Anspruch 1, wobei in Schritt (c) die Säule mit wässrigem Ethanol in
einer Konzentration von 40 - 95 % eluiert wird.
11. Verfahren nach Anspruch 9 oder 10, wobei die Konzentration des niederen C1- ~ C5-Alkohols oder des wässrigen Ethanols 60 - 95 % beträgt.
12. Verfahren nach Anspruch 10, wobei die Konzentration des wässrigen Ethanols 95 % beträgt.
1. Procédé pour la préparation d
'acide salvianolique total, comprenant les étapes consistant :
a. à extraire du Danshen avec de l'eau et à acidifier l'extrait et filtrer ;
b. à appliquer ledit extrait de Danshen sur une colonne de polyamide, laver la colonne
avec de l'eau jusqu'à une condition neutre, écarter les produits de lavage, éluer
la colonne de polyamide avec une solution aqueuse basique faible, et à recueillir
les fractions ;
c. à appliquer les fractions basiques de l'étape (b) sur une colonne de résine d'adsorption
macroporeuse de type styrène, après avoir acidifié les fractions, laver d'abord la
colonne avec de l'eau jusqu'à une condition neutre, écarter les produits de lavage
puis à éluer la colonne avec un alcool inférieur hydraté ou anhydre ; l'éluant étant
recueilli, concentré sous pression réduite jusqu'à disparition de l'alcool, et séché.
2. Procédé selon la revendication 1, dans lequel l'extraction dans l'étape (a) par de
l'eau en chauffant est répétée 2-4 fois, et pendant 0,5-2 h chacune.
3. Procédé selon la revendication 1, dans lequel la température pour ladite extraction
de l'étape (a) par de l'eau est de 60-100 °C.
4. Procédé selon la revendication 1, dans lequel la température pour ladite extraction
de l'étape (a) par de l'eau est de 90-100 °C.
5. Procédé selon la revendication 1, dans lequel ledit extrait de l'étape (a) est ajusté
avec un acide jusqu'à une valeur de pH inférieure à 4, et les fractions basiques de
l'étape (c) sont acidifiées avec un acide jusqu'à une valeur de pH inférieure à 4.
6. Procédé selon la revendication 1, dans lequel ledit extrait de l'étape (a) est acidifié
avec un acide jusqu'à une valeur de pH inférieure à 2, et les fractions basiques de
l'étape (c) sont acidifiées avec de l'acide chlorhydrique ou de l'acide sulfurique
jusqu'à une valeur de pH inférieure à 2.
7. Procédé selon la revendication 1, dans lequel, dans l'étape (b), on utilise 0,01-2
% de la solution aqueuse basique faible en tant qu'éluant.
8. Procédé selon la revendication 1, dans lequel, dans l'étape (b), on utilise 0,08-0,5
% d'une solution aqueuse de bicarbonate de sodium en tant qu'éluant.
9. Procédé selon la revendication 1, dans lequel l'alcool inférieur en C1-C5 hydraté ou anhydre est utilisé en tant qu'éluant dans l'étape (c).
10. Procédé selon la revendication 1, dans lequel, dans l'étape (c), la colonne est éluée
avec de l'éthanol aqueux ayant une concentration de 40-95 %.
11. Procédé selon la revendication 9 ou 10, dans lequel la concentration de l'alcool inférieur
en C1-C5 ou de l'éthanol aqueux est de 60-95 %.
12. Procédé selon la revendication 10, dans lequel la concentration de l'éthanol aqueux
est de 95 %.