CN106337093A - Sugar production method of ultra-low sulfur white granulated sugar - Google Patents

Sugar production method of ultra-low sulfur white granulated sugar Download PDF

Info

Publication number
CN106337093A
CN106337093A CN201610776047.6A CN201610776047A CN106337093A CN 106337093 A CN106337093 A CN 106337093A CN 201610776047 A CN201610776047 A CN 201610776047A CN 106337093 A CN106337093 A CN 106337093A
Authority
CN
China
Prior art keywords
sugar
liquid
production method
sacchari sinensis
caulis sacchari
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.)
Pending
Application number
CN201610776047.6A
Other languages
Chinese (zh)
Inventor
黄光农
张振月
梁冰
苏杏严
黎海关
罗香忠
农健
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.)
GUANGXI STATE FARMS SUGAR INDUSTRIAL GROUP CHANGLING SUGAR MANUFACTURING Co Ltd
Original Assignee
GUANGXI STATE FARMS SUGAR INDUSTRIAL GROUP CHANGLING SUGAR MANUFACTURING 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 GUANGXI STATE FARMS SUGAR INDUSTRIAL GROUP CHANGLING SUGAR MANUFACTURING Co Ltd filed Critical GUANGXI STATE FARMS SUGAR INDUSTRIAL GROUP CHANGLING SUGAR MANUFACTURING Co Ltd
Priority to CN201610776047.6A priority Critical patent/CN106337093A/en
Publication of CN106337093A publication Critical patent/CN106337093A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B10/00Production of sugar juices
    • C13B10/02Expressing juice from sugar cane or similar material, e.g. sorghum saccharatum
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B20/00Purification of sugar juices
    • C13B20/14Purification of sugar juices using ion-exchange materials
    • C13B20/146Purification of sugar juices using ion-exchange materials using only anionic ion-exchange material
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B20/00Purification of sugar juices
    • C13B20/16Purification of sugar juices by physical means, e.g. osmosis or filtration
    • C13B20/165Purification of sugar juices by physical means, e.g. osmosis or filtration using membranes, e.g. osmosis, ultrafiltration
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B20/00Purification of sugar juices
    • C13B20/18Purification of sugar juices by electrical means
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B30/00Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
    • C13B30/002Evaporating or boiling sugar juice
    • CCHEMISTRY; METALLURGY
    • C13SUGAR INDUSTRY
    • C13BPRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
    • C13B30/00Crystallisation; Crystallising apparatus; Separating crystals from mother liquors ; Evaporating or boiling sugar juice
    • C13B30/02Crystallisation; Crystallising apparatus

Abstract

The invention relates to the field of sugar production, in particular to a sugar production method of ultra-low sulfur white granulated sugar. The sugar production method comprises the following steps: pressing sugarcane to obtain sugarcane juice; adding sodium hydroxide to the sugarcane juice to regulate pH of the sugarcane juice to 5-6; heating the sugarcane juice to 60-65 DEG C; performing flocculation decolorization to obtain clarified liquid; performing membrane separation on the clarified liquid to remove impurities in the clarified liquid and to obtain purified liquid; using acid for regulating the purified liquid to be neutral; performing electrodialysis on the purified liquid for removing salt formed by acid and alkali; then concentrating to obtain concentrated liquid; performing strong alkaline anion exchange on the concentrated liquid to remove pigments and ash; performing weak acid cation exchange for desalination; finally, evaporating and concentrating the obtained sugar liquid, combining and crystallizing to obtain the white granulated sugar. The sugar production method of ultra-low sulfur white granulated sugar provided by the invention is simple to operate, needs no sulfur during decolorization, and reduces sulfur component in the product.

Description

The Closed Circulation in Sugar Production method of super-low sulfur white sugar
Technical field
The present invention relates to sugared production field is and in particular to the Closed Circulation in Sugar Production method of super-low sulfur white sugar.
Background technology
General cane sugar factory is divided into carbonatation process and sulfurous method, and two methods are required for adding to some extent sulfur dioxide Decoloured, this process is referred to as stove drying.Stove drying is carried out at twice, and the clear juice stove drying before evaporation is to reduce colour and suppressing high The stylish pigment of temperature evaporation generates, and the syrup stove drying after evaporation is conducive to reducing the colour boiling sugared clean plasm further, produces symbol Close the finished product white sugar of colour index.
Stove drying has the pros and cons effect to product quality, first, stove drying can reduce commerieal sugar colour;Second, sulfur The smoked so2 content (abbreviation sulfur content) that increased commerieal sugar.How to solve this paradox of stove drying, be allowed to both reduce finished product Fried sugar value does not increase the sulfur content of commerieal sugar again, be Closed Circulation in Sugar Production for many years faced by very stubborn problem.
Content of the invention
The present invention provides a kind of Closed Circulation in Sugar Production method of super-low sulfur white sugar.
The technical solution adopted in the present invention is:
The Closed Circulation in Sugar Production method of super-low sulfur white sugar, including procedure below:
Caulis Sacchari sinensis are squeezed, and obtain Caulis Sacchari sinensis juice, and the ph that Caulis Sacchari sinensis juice adds sodium hydroxide regulation Caulis Sacchari sinensis juice is 5~6, Caulis Sacchari sinensis juice It is heated to 60~65 DEG C, carry out flocculation decoloration, obtain clear liquor;
Clear liquor carries out the impurity that membrance separation removes in clear liquor, obtains pure liquid, and the acid of pure liquid adjusts neutral;
Pure liquid carries out electrodialysis, and the salinity that soda acid is formed is sloughed, and is then concentrated, and obtains concentrated solution;
Concentrated solution carries out strong alkalinity anion exchange and removes depigmentation and ash, then carries out Subacidity cation exchange desalination; The sugar liquid evaporation and concentration finally obtaining, combination crystallization obtains white sugar.
The Closed Circulation in Sugar Production method of the super-low sulfur white sugar that the present invention provides, simple to operate, do not need sulfur in decolorization, fall Sulfur composition in low product.
Specific embodiment
The present invention is further illustrated with reference to embodiments, but the present invention is not limited only to these embodiments, not On the premise of departing from present inventive concept, any improvement made is within the scope of the present invention.
The Closed Circulation in Sugar Production method of super-low sulfur white sugar, including procedure below:
Caulis Sacchari sinensis are squeezed, and obtain Caulis Sacchari sinensis juice, and the ph that Caulis Sacchari sinensis juice adds sodium hydroxide regulation Caulis Sacchari sinensis juice is 5~6, Caulis Sacchari sinensis juice It is heated to 60~65 DEG C, carry out flocculation decoloration, obtain clear liquor;
Clear liquor carries out the impurity that membrance separation removes in clear liquor, obtains pure liquid, and the acid of pure liquid adjusts neutral;
Pure liquid carries out electrodialysis, and the salinity that soda acid is formed is sloughed, and is then concentrated, and obtains concentrated solution;
Concentrated solution carries out strong alkalinity anion exchange and removes depigmentation and ash, then carries out Subacidity cation exchange desalination; The sugar liquid evaporation and concentration finally obtaining, combination crystallization obtains white sugar.

Claims (1)

1. super-low sulfur white sugar Closed Circulation in Sugar Production method it is characterised in that: include procedure below:
Caulis Sacchari sinensis are squeezed, and obtain Caulis Sacchari sinensis juice, and the ph that Caulis Sacchari sinensis juice adds sodium hydroxide regulation Caulis Sacchari sinensis juice is 5 ~ 6, and Caulis Sacchari sinensis juice heats To 60 ~ 65 DEG C, carry out flocculation decoloration, obtain clear liquor;
Clear liquor carries out the impurity that membrance separation removes in clear liquor, obtains pure liquid, and the acid of pure liquid adjusts neutral;
Pure liquid carries out electrodialysis, and the salinity that soda acid is formed is sloughed, and is then concentrated, and obtains concentrated solution;
Concentrated solution carries out strong alkalinity anion exchange and removes depigmentation and ash, then carries out Subacidity cation exchange desalination;Finally The sugar liquid evaporation and concentration obtaining, combination crystallization obtains white sugar.
CN201610776047.6A 2016-08-31 2016-08-31 Sugar production method of ultra-low sulfur white granulated sugar Pending CN106337093A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610776047.6A CN106337093A (en) 2016-08-31 2016-08-31 Sugar production method of ultra-low sulfur white granulated sugar

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610776047.6A CN106337093A (en) 2016-08-31 2016-08-31 Sugar production method of ultra-low sulfur white granulated sugar

Publications (1)

Publication Number Publication Date
CN106337093A true CN106337093A (en) 2017-01-18

Family

ID=57824007

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610776047.6A Pending CN106337093A (en) 2016-08-31 2016-08-31 Sugar production method of ultra-low sulfur white granulated sugar

Country Status (1)

Country Link
CN (1) CN106337093A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103937913A (en) * 2014-04-20 2014-07-23 厦门世达膜科技有限公司 White granulated sugar production technology
CN104805226A (en) * 2015-04-27 2015-07-29 广西大学 Sugar manufacture clarification process
CN106282419A (en) * 2016-08-10 2017-01-04 云南省轻工业科学研究院 A kind of Caulis Sacchari sinensis juice purification process in Closed Circulation in Sugar Production

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103937913A (en) * 2014-04-20 2014-07-23 厦门世达膜科技有限公司 White granulated sugar production technology
CN104805226A (en) * 2015-04-27 2015-07-29 广西大学 Sugar manufacture clarification process
CN106282419A (en) * 2016-08-10 2017-01-04 云南省轻工业科学研究院 A kind of Caulis Sacchari sinensis juice purification process in Closed Circulation in Sugar Production

Similar Documents

Publication Publication Date Title
CN103725802B (en) The technique that a kind of sucrose is refining
CN102676707B (en) Efficient and energy-saving xylose producing process
CN102659855B (en) Energy-saving environment-friendly sucrose production process
CN103981290A (en) Process for preparing sugar from cane
CN102976923B (en) New process for extracting lactic acid from lactic acid fermentation liquid
CN102260753B (en) Method for clearing, decoloring and decontaminating sugar juice
CN103866052A (en) Sulfur-free clarifying method for cane sugar manufacture
CN105063247B (en) A kind of sugar refining technology using multistage membrane filtration technique purification Cane Mixed Juice
CN105483181A (en) Preparation method of high-purity glucose
CN104805226A (en) Sugar manufacture clarification process
CN102031315A (en) Method for regenerating sugar making decolorized and decalcified resin and method for recycling regeneration waste liquid
CN112876520A (en) Preparation method of high-quality arabinose, galactose, rhamnose and glucuronic acid
CN111919908A (en) Preparation method of desalted whey powder
CN102977163A (en) Industrialized preparation method of stevioside
CN109527523A (en) A kind of fructose syrup, glucose is collinear production method
CN108203739A (en) A kind of process for purification of medical cane sugar
CN105755179A (en) Cane sugar manufacturing method
AU2010318820B2 (en) Method for producing white sugar, light brown sugar and dark brown sugar using direct recovery process
CN106337093A (en) Sugar production method of ultra-low sulfur white granulated sugar
CN108640816B (en) Refining process for inositol filtrate by high-temperature rapid ion exchange
CN107556162B (en) Method for continuously extracting erythritol
CN108893510A (en) A kind of compounding method of the fructose syrup made of plant amylum hydrolysis and isomerization
JP2024507212A (en) Xylitol/caramel color co-production system and method using xylose mother liquor
CN107267673A (en) Cane sugar manufacture technique
ZA200210223B (en) Process for preheating colored aqueous sugar solutions to produce a low colored crystallized sugar.

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20170118

RJ01 Rejection of invention patent application after publication