CN202543166U - Distilling processing concentrator for sweet orange oil - Google Patents

Distilling processing concentrator for sweet orange oil Download PDF

Info

Publication number
CN202543166U
CN202543166U CN2012201688797U CN201220168879U CN202543166U CN 202543166 U CN202543166 U CN 202543166U CN 2012201688797 U CN2012201688797 U CN 2012201688797U CN 201220168879 U CN201220168879 U CN 201220168879U CN 202543166 U CN202543166 U CN 202543166U
Authority
CN
China
Prior art keywords
orange oil
sweet orange
crystallizing
distilling
freezing
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 - Lifetime
Application number
CN2012201688797U
Other languages
Chinese (zh)
Inventor
张长征
马海波
黄战鏖
钱正刚
纪建平
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.)
Shanghai Wanxiang Flavors & Fragrances Co Ltd
Original Assignee
Shanghai Wanxiang Flavors & Fragrances Co Ltd
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 Shanghai Wanxiang Flavors & Fragrances Co Ltd filed Critical Shanghai Wanxiang Flavors & Fragrances Co Ltd
Priority to CN2012201688797U priority Critical patent/CN202543166U/en
Application granted granted Critical
Publication of CN202543166U publication Critical patent/CN202543166U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The utility model discloses a distilling processing concentrator for sweet orange oil, which comprises a distilling tower and is characterized by further comprising a crystallizing chamber and a drum centrifugal machine, wherein the sweet orange oil distilled by the distilling tower is conveyed to the crystallizing chamber for freezing and crystallizing through a first pipeline, and the concentrated sweet orange oil after being frozen and crystallized is conveyed to the drum centrifugal machine for centrifuging through a second pipeline, thereby obtaining an end product. The drum centrifugal machine with a rotating speed at 17000 rpm is adopted for de-waxing by the distilling processing concentrator for the sweet orange oil, the centrifuging efficiency is high and the output is increased by two times. The crystallizing chamber is additionally arranged in the distilling processing concentrator for the sweet orange oil and the de-waxing treatment is performed after the freezing and crystallizing treatment, so that the product is free from waxy material even in winter.

Description

Sweet orange oil distillation processing thickening equipment
Technical field
The utility model relates to sweet orange oil distillation processing thickening equipment.
Background technology
Referring to Fig. 1, when sweet orange oil concentrated sweet orange oil through distillation processing, the wax in the product was also concentrated thereupon, after envrionment temperature reduces, was exactly that flocculent precipitate occurs.Common dewaxing technique is that the wax in the finished product is filtered out through flame filter press 1, but the thickness very of the wax in the sweet orange oil, thus slow with flame filter press 1 filtration velocity, and production process also can bring the filter paper fibre of trace into, influences the quality of product.When produce winter in addition, still have wax to occur in the product.
The utility model content
The utility model technical problem to be solved is through existing problem in the concentrated sweet orange oil method of distillation processing a kind of sweet orange oil distillation processing thickening equipment to be provided to existing sweet orange oil.
The utility model technical problem to be solved can realize through following technical scheme:
Sweet orange oil distillation processing thickening equipment; Comprise distillation tower; It is characterized in that; Also comprise between crystallization and the rotary drum whizzer, distillation tower distillatory sweet orange oil is delivered to freezing and crystallizing between crystallization through first pipeline, and the concentrated sweet orange oil behind the freezing and crystallizing is delivered to the centrifugal finished product that gets of rotary drum whizzer through second pipeline.
Owing to adopted technical scheme as above, the utility model employing rotating speed is that 17000 rev/mins rotary drum whizzer dewaxes, and separation efficiency is high, and output has improved twice.The utility model adding finishes intergranular, carries out dewaxing treatment behind the freezing and crystallizing again, occurs even product does not also have wax in winter.
Description of drawings
Fig. 1 concentrates the process flow sheet of sweet orange oil for existing sweet orange oil distillation processing.
Fig. 2 is the utility model sweet orange oil distillation processing thickening equipment and process flow sheet.
Embodiment
Further specify the utility model below in conjunction with accompanying drawing and embodiment.
Referring to Fig. 2; The sweet orange oil distillation processing thickening equipment that provides among the figure; Comprise between distillation tower 100, crystallization 200 and rotary drum whizzer 300, single times of sweet orange oil gets into distillation tower 100 and carries out rectification, and distillatory sweet orange oil (5 or 10 times) finished product is delivered between crystallization 200 through pipeline 400 and is refrigerated to-5 ℃; Wax is separated out in crystallization, and it is 17000 rev/mins of rotary drum whizzers, the 300 centrifugal finished products that get that the concentrated sweet orange oil behind the freezing and crystallizing is delivered to rotating speed through pipeline 500.

Claims (1)

1. thickening equipment is processed in the sweet orange oil distillation; Comprise distillation tower; It is characterized in that; Also comprise between crystallization and the rotary drum whizzer, distillation tower distillatory sweet orange oil is delivered to freezing and crystallizing between crystallization through first pipeline, and the concentrated sweet orange oil behind the freezing and crystallizing is delivered to the centrifugal finished product that gets of rotary drum whizzer through second pipeline.
CN2012201688797U 2012-04-19 2012-04-19 Distilling processing concentrator for sweet orange oil Expired - Lifetime CN202543166U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012201688797U CN202543166U (en) 2012-04-19 2012-04-19 Distilling processing concentrator for sweet orange oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012201688797U CN202543166U (en) 2012-04-19 2012-04-19 Distilling processing concentrator for sweet orange oil

Publications (1)

Publication Number Publication Date
CN202543166U true CN202543166U (en) 2012-11-21

Family

ID=47163831

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2012201688797U Expired - Lifetime CN202543166U (en) 2012-04-19 2012-04-19 Distilling processing concentrator for sweet orange oil

Country Status (1)

Country Link
CN (1) CN202543166U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104560394A (en) * 2014-12-29 2015-04-29 上海万香日化有限公司 Method for comprehensively utilizing sweet orange oil terpene by-products
CN116106057A (en) * 2022-10-18 2023-05-12 广东省农业科学院果树研究所 Quick and efficient collection and analysis method for fruit surface wax cream

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104560394A (en) * 2014-12-29 2015-04-29 上海万香日化有限公司 Method for comprehensively utilizing sweet orange oil terpene by-products
CN116106057A (en) * 2022-10-18 2023-05-12 广东省农业科学院果树研究所 Quick and efficient collection and analysis method for fruit surface wax cream
CN116106057B (en) * 2022-10-18 2023-09-19 广东省农业科学院果树研究所 Quick and efficient collection and analysis method for fruit surface wax cream

Similar Documents

Publication Publication Date Title
MD961Y (en) Method for producing inulin and other fructan-containing products from Jerusalem artichoke
CN101985416A (en) Refining technology for producing long carbon chain dicarboxylic acid by using biological fermentation process
CN202543166U (en) Distilling processing concentrator for sweet orange oil
CN103554250A (en) Method for extracting phycocyanin
CN104059865B (en) A kind of streptococcus zooepidemicus and prepare the production technology of hyaluronic acid with it
CN107383135A (en) The method that β thymidines are isolated and purified from zymotic fluid
CN103667381A (en) Method for improving yield of arginine
CN102838624A (en) Method for purifying clavulanic acid from fermentation liquor
CN105219889A (en) A kind of method of membrane separation purification starch saccharificating liquid
CN104877390A (en) Preparation method of black carrot pigment with high purity
CN101875598B (en) Separation method of 1, 3-propylene glycol fermentation liquor
CN103214113A (en) Chromatographic separation method of sodium chloride and sodium glycollate in waste water in production process of sodium carboxy methyl cellulose
CN203650574U (en) Aloe cutting and filtering device
CN106554273B (en) Method for purifying long-chain dicarboxylic acid in fermentation liquor
CN102931442B (en) A kind of method of abnormity volume needle winding battery
CN102249865B (en) Method for purifying high-purity transacomhole
CN101973840A (en) Method for separating durene by freezing crystallization
CN206260794U (en) Spices stem-leaf separating machine
CN103114328B (en) The preparation method of 8 cun of < 110 > magnetic Czochralski monocrystalline
CN100494394C (en) Method for preparing raw material containing pleuromutilin for tiamulin production process
CN203985115U (en) The process equipment of corn
CN205074222U (en) Phosphorus fertilizer processing continuous operation screen cloth plug -hole adjusting device
CN104495770A (en) Method for purifying wet process phosphoric acid by crystallization in extraction process
CN102676705A (en) New process for separating and purifying starch sugar mother solution
CN105669351A (en) Crude anthracene production method and device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Distilling processing concentrator for sweet orange oil

Effective date of registration: 20131122

Granted publication date: 20121121

Pledgee: Bank of Shanghai Limited by Share Ltd Pudong branch

Pledgor: Shanghai Wanxiang Flavors & Fragrances Co., Ltd.

Registration number: 2013310000070

PLDC Enforcement, change and cancellation of contracts on pledge of patent right or utility model
PC01 Cancellation of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20210917

Granted publication date: 20121121

Pledgee: Bank of Shanghai Limited by Share Ltd. Pudong branch

Pledgor: SHANGHAI WANXIANG FLAVORS & FRAGRANCES Co.,Ltd.

Registration number: 2013310000070

CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20121121