CN1013579B - Process for producing rutin - Google Patents

Process for producing rutin

Info

Publication number
CN1013579B
CN1013579B CN 87103731 CN87103731A CN1013579B CN 1013579 B CN1013579 B CN 1013579B CN 87103731 CN87103731 CN 87103731 CN 87103731 A CN87103731 A CN 87103731A CN 1013579 B CN1013579 B CN 1013579B
Authority
CN
China
Prior art keywords
rutin
water
technology
ammonium bicarbonate
producing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
CN 87103731
Other languages
Chinese (zh)
Other versions
CN1030764A (en
Inventor
刘长林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing University of Technology
Original Assignee
Beijing University of Technology
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing University of Technology filed Critical Beijing University of Technology
Priority to CN 87103731 priority Critical patent/CN1013579B/en
Publication of CN1030764A publication Critical patent/CN1030764A/en
Publication of CN1013579B publication Critical patent/CN1013579B/en
Expired legal-status Critical Current

Links

Landscapes

  • Saccharide Compounds (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

The present invention relates to a technology for producing rutin, which is a chemical technology for extracting rutin form buds of Chinese scholartree. The technology is characterized in that a small amount of lime water is added instead of lime milk water to aqueous ammonium bicarbonate solution to be steamed, cool water is used instead of warmed water to wash raw materials, and crystallized rutin is not washed by using acid water. Ammonium bicarbonate with a small amt. Compared with a conventional technology for producing rutin. The technology has obvious advantages of high rutin yield, good quality, little energy consumption, etc.

Description

Process for producing rutin
The rutin production method is meant a kind of chemical industry method of extracting rutin from the sophora bud.
Rutin can also can be used as the intermediate of medicine, dyestuff and the additive of food directly as medicine.Traditional process for producing rutin is earlier the raw material sophora bud to be pulverized, through making the finished product rutin after the operations such as warm water washing, the boiling of hot lime whey, purification, neutralization, cooling, filtration, pickling, washing, oven dry, pulverizing, sometimes also to just can obtain qualified product through the treating process second time.The shortcoming of this technical process is, rutin yield is low, only is 8%-12%, and it is faint yellow that product is, and residue on ignition is often higher.For this reason, proposed production method of the present invention, it is characterized in that,, added a small amount of liming with ammonium bicarbonate aqueous solution and come the boiling of replacing lime whey, when the washing sophora bud, replaced warm water with cold water at cooking process; When the wash crystallization rutin, remove sour water from.The trial production result, rutin yield can reach 13%-17%, has improved 20%-40% than traditional technology, and quality product has also improved, and especially residue on ignition obviously descends, and the finished product rutin is distinctive little green-yellow; Owing to use cold water washing, can save energy about 50%, reduced the consumption of industrial chemicals, simplified operating process.
Embodiment:
Sophora bud 50kg after having pulverized adds water 1000kg and under agitation washs, totally three times.Add the about 1000kg of water more under agitation, begin to add steam and heat up, it is some to add about 15kg saturated limewater and ammonium bicarbonate aqueous solution simultaneously.In adding the diminishing process, ceaselessly stir, and the pH value of limit edged inspection extracting solution, make when extracting solution seethes with excitement, to keep pH8.5-9.0, add the 0.2kg borax again.Be incubated half an hour under boiling, leach sophora bud slag, soup carries out purifying treatment with pressure by 10 layers of cloth bag.In soup, add the dilute hydrochloric acid neutralization, equal 6 to the pH value of solution, and cooling under agitation, placement is spent the night, and makes the rutin precipitation complete.Leach precipitation with the plate and frame filter, washed about 2.5 hours with softening water, after the centrifuge dehydration, oven dry through pulverizing, promptly gets the rutin finished product again in about 80 ℃.
Above-mentioned sophora bud slag adds water 800kg again, saturated limewater 2kg, and borax 0.2kg repeats above operating process, obtains the rutin finished product once more.
Merge the above-mentioned two altogether 7.1kg of rutin finished product that take second place, yield 14.2%, product is by " Drug Standard of Ministry of Public Health of the Peoples Republic of China (1963) " chemical examination, rutin content 95.1%, moisture 8.7%, insolubles 5.5mg in the ethanol, residue on ignition 0.42%.

Claims (2)

1, a kind of chemical industry method of from the sophora bud, extracting rutin, traditional technical process is, sophora bud pulverizing → warm water washing → lime emulsification boiling → purification → neutralization → cooling → filtration → pickling → wash → dry → pulverize the finished product rutin, it is characterized in that, at cooking process, with be ammonium bicarbonate aqueous solution and a small amount of liming, the pH value of using bicarbonate of ammonia control solution is between 8.5-9.0.
2, according to the rutin production method of claim 1, wherein washing procedure is characterized in that carrying out with cold water when washing material, only carries out with softening water during the wash crystallization rutin.
CN 87103731 1987-05-25 1987-05-25 Process for producing rutin Expired CN1013579B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 87103731 CN1013579B (en) 1987-05-25 1987-05-25 Process for producing rutin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 87103731 CN1013579B (en) 1987-05-25 1987-05-25 Process for producing rutin

Publications (2)

Publication Number Publication Date
CN1030764A CN1030764A (en) 1989-02-01
CN1013579B true CN1013579B (en) 1991-08-21

Family

ID=4814559

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 87103731 Expired CN1013579B (en) 1987-05-25 1987-05-25 Process for producing rutin

Country Status (1)

Country Link
CN (1) CN1013579B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9827262B2 (en) 2012-10-22 2017-11-28 Alps Pharmaceuticals, Ind. Co., Ltd. Rutin-rich extract and method of making same

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1052983C (en) * 1998-07-28 2000-05-31 中国科学院昆明植物研究所 Melim sulfate compound
CN102807596A (en) * 2012-08-23 2012-12-05 四川省砚山中药饮片有限公司 Method for extracting rutin
CN105949255A (en) * 2016-05-11 2016-09-21 驻马店天中生物科技有限公司 Extracting method of rutin
CN111635443A (en) * 2020-06-15 2020-09-08 深圳市蜜踪生物科技有限公司 Sophora flower extraction process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9827262B2 (en) 2012-10-22 2017-11-28 Alps Pharmaceuticals, Ind. Co., Ltd. Rutin-rich extract and method of making same

Also Published As

Publication number Publication date
CN1030764A (en) 1989-02-01

Similar Documents

Publication Publication Date Title
US2051017A (en) Process for producing from plant materials protein decomposition products, mineral salts, and soluble carbohydrates
CN101817857A (en) Process for extracting rutin from sophora japonica
CN102134260A (en) Method for preparing phytic acid
CN1013579B (en) Process for producing rutin
CN106117038B (en) A kind of technique that calcium lactate is produced using nisin waste water
JPS6052785B2 (en) Soy milk production method
CN102690191A (en) Method for producing calcium lactate by taking duck egg shell as raw material
CN1128813C (en) Pectin producing method
NO750859L (en)
CN103483403A (en) Circulating extraction method for extracting and purifying hesperidin from orange residues
CN106435047A (en) Method for preparing xylose from corncobs
CN1322805A (en) Soybean detergent and its production process
CN1036136C (en) Method for preparation of oligosaccharilde liquid from dregs of bean
CN1331867C (en) Preparation method of citric acid-amino acid calcium
CN1045784A (en) Speiss in the camptothecine production process is handled
US1543763A (en) Decolorizing carbon and process of producing the same
CN1045965A (en) Non-refrigeration method is produced the technology of inositol
CN108642588B (en) Preparation method of feather protein liquid suitable for manufacturing feather protein fibers
CN107501109A (en) A kind of iminodiacetic acid (salt) acid treating Preparation Method
AT85397B (en) Process for the production of a condiment from milk.
CN103059164A (en) Pectin extracting process
CN1406916A (en) Inositol producing process
SU1693011A1 (en) Method of producing collagen hydrolyzate from chrome leather waste
CN106912665A (en) A kind of preparation method of chrysanthemum sesame oil brown sugar
CN106306062A (en) Peanut bean curd production method

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C13 Decision
GR02 Examined patent application
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee