CN1232622C - Technique for extracting rhodamine oil - Google Patents

Technique for extracting rhodamine oil Download PDF

Info

Publication number
CN1232622C
CN1232622C CN 200410029668 CN200410029668A CN1232622C CN 1232622 C CN1232622 C CN 1232622C CN 200410029668 CN200410029668 CN 200410029668 CN 200410029668 A CN200410029668 A CN 200410029668A CN 1232622 C CN1232622 C CN 1232622C
Authority
CN
China
Prior art keywords
rose
water
oil
steam
close type
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 - Fee Related
Application number
CN 200410029668
Other languages
Chinese (zh)
Other versions
CN1563311A (en
Inventor
邱云彪
高延厅
胡秀麟
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.)
Zhejiang KAIDI Pharmaceutical Chemical Machinery Co., Ltd.
Original Assignee
邱云彪
高延厅
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 邱云彪, 高延厅 filed Critical 邱云彪
Priority to CN 200410029668 priority Critical patent/CN1232622C/en
Publication of CN1563311A publication Critical patent/CN1563311A/en
Application granted granted Critical
Publication of CN1232622C publication Critical patent/CN1232622C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Fats And Perfumes (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The present invention discloses a technology for extracting rose essence oil, which is characterized in that rose flowers and water are mixed and placed in a quickly-opened distillation tank; then steam is led in a jacket of the quickly-opened distillation tank, and the rose flowers and the water are stirred and heated in the quickly-opened distillation tank by a stirring device; after steam generated in the quickly-opened distillation tank is twice distilled by a distillation column, and the steam is condensed by a condenser and cooled by a cooler; secondary water-oil separating is carried out; finally the rose essence oil is obtained. In the present invention, the steam is led in the jacket of the distillation tank to be heated. Because of large heating area and high heating speed, after the rose flowers and the water in the distillation tank are heated, heating reaction is carried out in a dynamic state under the condition that the rose flowers and the water are stirred by the stirring device. Thus, the internal quality of the rose flowers is not influenced, and the original properties and the transparence of the rose flowers are preserved. After secondary water-oil separating is adopted, oil and water are thoroughly separated from each other. Thereby, the quality, the output and the purity of the rose essence oil are increased.

Description

A kind of extracting method of Flos Rosae Rugosae quintessence oil
[technical field]
What the present invention relates to is a kind of extracting method of Chinese medicinal materials, and what be specifically related to is a kind of Rose extracts essential oil method.
[background technology]
In the prior art, Rose extracts essential oil method is Rose and water to be presented in the inferior pyramidal retort directly water is heated, and the steam after the heating separates obtaining Flos Rosae Rugosae quintessence oil then by the shell-and tube condenser condensation by water-and-oil separator.This extracting method is owing to adopted the retort of last inferior pyramidal, and directly feed retort with dry steam and heat, residue after distillation finishes, can only be with manually in the lateral hole of retort, excavating, Rose is attached on the heating pipe because the coking phenomenon that high temperature produced, clean very difficult, very time-consuming, owing to adopt dry steam not through separating and purifying, in the thermal process reactor of whole static state, thermal source in the steam and impurity have directly damaged composition and the character of Rose, make the rose oil muddiness that distills out contain smell of urine flavor again, still residual stain in the oil has influenced the quality of rose oil, and this method adopts a shell-and tube condenser to cool off, make the gas-liquid that has rose oil enter condenser and can not get cooling off completely, cause the loss of rose oil gas-liquid, adopt simultaneously a table oil water separator carry out he from, make profit can not get separating fully, directly influenced the output and the purity of rose oil.How to make the rose oil of extraction keep original character of Rose and composition, and make that its transparency is good, quality and output height, be that those skilled in the art want to solve and an insoluble difficult problem always.
[summary of the invention]
In view of problems of the prior art, the object of the present invention is to provide a kind of rose oil that makes to keep original character and composition, improve the extracting method of quality, output and the purity of rose oil product.For achieving the above object, the present invention takes following scheme to finish: the extracting method of this Flos Rosae Rugosae quintessence oil, it is characterized in that Rose and water mixing are inserted in the pneumatic open and close type retort, then steam is fed in the chuck of pneumatic open and close type retort, heat while stirring in pneumatic open and close type retort with whipping appts, the steam that produces in the pneumatic open and close type retort is through behind the second distillation of distillation column, pass through condenser condenses, the water cooler cooling, carry out secondary oily water separation again, obtain Flos Rosae Rugosae quintessence oil at last, described pneumatic open and close type retort is to be provided with cylinder and connecting rod in the outside of tank body, and described cylinder and connecting rod are by hinged-support and rod hinge connection, to the retort distillation test residue, press pneumatically operated switch, the capping of discharge port is opened fully, and with the disposable discharge of residue, described condenser and water cooler are rolled plate.
The present invention feeds steam in the chuck of retort and heats, because heating-surface area is big, rate of heating is fast, after Rose in the retort and water are heated, under the stirring of whipping appts, thermal response is carried out under dynamical state, can not make the Rose in the retort produce coking phenomenon, and can not have influence on Rose intrinsic quality, keep original fragrance of Rose and transparency; Adopt the retort of pneumatic open and close type, distillation test residue can disposablely be discharged, save time very much, and it is convenient to clean, adopt board-like condenser, condensation area is big, easy cleaning, with condensed gas-liquid again through supercooler, it is fully cooled off, can not run off, adopt secondary oily water separation simultaneously, oil is thoroughly separated with water, improved the output and the purity of Flos Rosae Rugosae quintessence oil.Adopt the extracting method of theme of the present invention, will bring positive economic benefit for the producer that extracts Flos Rosae Rugosae quintessence oil.
[description of drawings]
The present invention has following accompanying drawing:
Fig. 1 is a schema of the present invention.
[embodiment]
Accompanying drawing has been represented the implementation process of the inventive method, further describes each relevant details of embodiment below more in conjunction with the accompanying drawings.The extracting method of this Flos Rosae Rugosae quintessence oil, at first be that Rose and water mixing are inserted in the pneumatic open and close type retort, then steam is fed in the chuck of pneumatic open and close type retort, heat while stirring in pneumatic open and close type retort with whipping appts, the steam that produces in the pneumatic open and close type retort is through behind the second distillation of distillation column, by condenser condenses, water cooler cooling, carry out secondary oily water separation again, obtain the Flos Rosae Rugosae quintessence oil product at last; In heat-processed, temperature should be controlled at 100~120 ℃; Be back to again in retort and the distillation column through the water after the secondary separation; The retort of described pneumatic open and close type is to be provided with cylinder and connecting rod in the outside of tank body, described cylinder is by hinged-support and rod hinge connection, to the retort distillation test residue, as long as press pneumatically operated switch, the capping of discharge port is opened fully, with the disposable discharge of residue, save time very much, and clean conveniently; Described condenser and water cooler are rolled plate; Described rolled plate condenser and water cooler are the cooling tubes that adopts rolled plate in condenser and water cooler; After the cooling of this two-stage, make the gas-liquid cooling fully, can not run off, and provide good basis for the oily water separation of subsequent processing; Because the special proportion of rose oil in order fully to collect the Rose essential oil, so adopt secondary oily water separation, makes oil thoroughly separate with water, has improved the output and the purity of Flos Rosae Rugosae quintessence oil; Equipment in the inventive method all adopts the fine stainless material, and not to Rose and water direct heating, and heating source is carried out in the chuck of retort, can not have influence on original character of Rose and composition, kept original fragrance of Rose and transparency.According to the Rose essential oil that the present invention extracts, quality, output and based on very high purity compared with prior art, have outstanding substantive distinguishing features and obvious improvement.

Claims (1)

1, a kind of extracting method of Flos Rosae Rugosae quintessence oil, it is characterized in that Rose and water mixing are inserted in the pneumatic open and close type retort, then steam is fed in the chuck of pneumatic open and close type retort, heat while stirring in pneumatic open and close type retort with whipping appts, the steam that produces in the pneumatic open and close type retort is through behind the second distillation of distillation column, condenser condenses and water cooler cooling by rolled plate, carry out secondary oily water separation again, obtain the Flos Rosae Rugosae quintessence oil product at last, described pneumatic open and close type retort is to be provided with cylinder and connecting rod in the outside of tank body, described cylinder is by hinged-support and rod hinge connection, to the retort distillation test residue, press pneumatically operated switch, the capping of discharge port is opened fully, with the disposable discharge of residue.
CN 200410029668 2004-03-31 2004-03-31 Technique for extracting rhodamine oil Expired - Fee Related CN1232622C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200410029668 CN1232622C (en) 2004-03-31 2004-03-31 Technique for extracting rhodamine oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200410029668 CN1232622C (en) 2004-03-31 2004-03-31 Technique for extracting rhodamine oil

Publications (2)

Publication Number Publication Date
CN1563311A CN1563311A (en) 2005-01-12
CN1232622C true CN1232622C (en) 2005-12-21

Family

ID=34480970

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200410029668 Expired - Fee Related CN1232622C (en) 2004-03-31 2004-03-31 Technique for extracting rhodamine oil

Country Status (1)

Country Link
CN (1) CN1232622C (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101721338B (en) * 2009-11-20 2012-08-22 甘肃农业大学 Cosmetic containing Rosa setate X R. rugosa water
CN102952644B (en) * 2012-12-06 2014-04-23 广西京桂香料有限公司 Device for extracting natural cinnamon oil
CN103146487B (en) * 2013-04-08 2014-07-30 云南绿宝香精香料股份有限公司 Water steam distillation device with duplex effects of extraction and separation
CN103740469B (en) * 2014-02-07 2015-04-08 郭永来 Steam distillation aromatic essential oil device
CN103897807B (en) * 2014-04-24 2016-02-17 银谷玫瑰科技有限公司 A kind of extracting method of Flos Rosae Rugosae quintessence oil
CN105199833B (en) * 2015-07-21 2019-02-05 广西大学 A kind of method for comprehensive processing of dried ginger slice and ginger oil
CN105001973B (en) * 2015-07-21 2019-02-12 广西壮族自治区林业科学研究院 A kind of consolidating processing equipment of dried ginger slice and ginger oil
CN108467792A (en) * 2018-05-17 2018-08-31 无锡市鹅湖玫瑰园艺文化有限公司 Rosa Damascana extraction element
CN108998244A (en) * 2018-08-08 2018-12-14 甘肃瑰隆生物科技有限公司 Rose ethereal oil extraction element
CN109749852A (en) * 2019-03-13 2019-05-14 甘肃瑰隆生物科技有限公司 The conveying charging process of rose in a kind of Rosa Damascana extraction process
CN111763571A (en) * 2020-07-08 2020-10-13 湖北瑞晟生物有限责任公司 Rose essential oil draws uses quick distillation plant
CN112500931B (en) * 2020-11-28 2021-09-21 上海丽舒丹医药科技有限公司 Preparation method of plant essential oil of acne-removing whitening skin care product

Also Published As

Publication number Publication date
CN1563311A (en) 2005-01-12

Similar Documents

Publication Publication Date Title
CN1232622C (en) Technique for extracting rhodamine oil
US4122104A (en) Process for extracting oils from oil containing raw materials
CN1679730A (en) Material of Chinese medicine extracting process and apparatus thereof
US11178888B2 (en) Production system and method for improving yield of bayberry juice
CN107057858A (en) Reduce the supercritical carbon dioxide method for extracting and device of extract acid value
CN110698325A (en) Production device and process for co-producing fuel ethanol and special grade edible alcohol
CN110229718A (en) A method of extracting essential oil from orange peel
CN102399257A (en) Method for extracting glycyrrhizic acid and liquorice flavonoid by using continuous countercurrent ultrasonic extraction machine
CN1710043A (en) Method for extracting passiflora seed oil from passiflora seeds
CN219363571U (en) Separation extraction element of extracting volatile oil from plant
CN1710042A (en) Method for extracting spine grape seed oil from spine grape seeds
CN2813047Y (en) Automatic control multifunction extracting thickener sets
CN1044568C (en) Distillation method for thermal sensitive material with simultaneous prodn. of light and heavy impurities
CN201952420U (en) Sugar extracting system of grain emulsion
US11477996B2 (en) Production process of soybean meal with high content of soluble proteins and product so obtained
CN201427937Y (en) Device for extracting fatty amine from fatty amine distillation residue
CN101343594A (en) Preparation method for rose hip or seed oil
CN1098859C (en) Process for supercritical carbon dioxide extracting and separating effective components of ginger
CN210495282U (en) Four-tower distillation and membrane separation integrated system
CN210933840U (en) Multifunctional extracting and concentrating integrated equipment
CN209500868U (en) Active ingredients from traditional Chinese medicinal extraction system
CN203033781U (en) Compound centrifugal film evaporator for preparing basic cupric carbonate
CN218232303U (en) Gas-liquid extraction device and rose essential oil preparation system using same
CN219217609U (en) Heat recovery device of reclaimed water stripping tower in butanol-octanol device
CN216786074U (en) Fragrant smell gas collection system of spices

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: ZHEJIANG KAIDI PHARMACEUTICAL CHEMICAL MACHINERY C

Free format text: FORMER OWNER: QIU YUNBIAO

Effective date: 20110830

Free format text: FORMER OWNER: GAO YANTING

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20110830

Address after: 325200 No. 7 Yaohua Road, eighteen industrial districts, Zhejiang, Ruian

Patentee after: Zhejiang KAIDI Pharmaceutical Chemical Machinery Co., Ltd.

Address before: 325200 Taiping stone 19, Anyang Town, Zhejiang, Ruian

Co-patentee before: Gao Yanting

Patentee before: Qiu Yunbiao

C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20051221

Termination date: 20130331