CN107164569A - It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour - Google Patents

It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour Download PDF

Info

Publication number
CN107164569A
CN107164569A CN201710359930.XA CN201710359930A CN107164569A CN 107164569 A CN107164569 A CN 107164569A CN 201710359930 A CN201710359930 A CN 201710359930A CN 107164569 A CN107164569 A CN 107164569A
Authority
CN
China
Prior art keywords
juice
white granulated
granulated sugar
sugarcane
crystal grain
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
CN201710359930.XA
Other languages
Chinese (zh)
Inventor
黄庆才
李权忠
何迪
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.)
Miyi Huasenty Co Ltd
Original Assignee
Miyi Huasenty 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 Miyi Huasenty Co Ltd filed Critical Miyi Huasenty Co Ltd
Priority to CN201710359930.XA priority Critical patent/CN107164569A/en
Publication of CN107164569A publication Critical patent/CN107164569A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Organic Chemistry (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The white granulated sugar production method of white granulated sugar colour is reduced the invention discloses a kind of, is comprised the following steps:The head of sugarcane is cut after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length and carries out sugar cane crushing, gained sugar-cane juice is crossed into 80~200 mesh sieves, Normal juice and sieving residue after being sieved;Normal juice after sieve is adjusted to pH6~6.5 in advance, it is heated to 55~65 DEG C, it is then added to neutralization reaction in stove drying averager, milk of lime regulation pH11~11.5 are added after reaction, it is heated to 90~100 DEG C, add after flocculant and enter settler sedimentation, obtain supernatant juice and mud juice, by mud juice by obtaining filtered juice after filter cloth, add SO2, crystallization and purification, dressing sieve crystal grain, dry crystal grain after supernatant juice and filtered juice are mixed through evaporation, again, by dried crystal grain by classifying except iron, packing, white granulated sugar is obtained.The white granulated sugar production method of the present invention, white granulated sugar sugaring efficiency is improved, and colour is substantially reduced.

Description

It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour
Technical field
The invention belongs to sugar refining field, and in particular to a kind of white granulated sugar production method of reduction white granulated sugar colour.
Background technology
The making of white granulated sugar is that raw material is manufactured mainly by sucrose, and the technique of cane sugar manufacture is a lot, than More common has lime method, sulfurous method, sulfurous method+syrup floatation and carbonatation process, either using which kind of method, its Principle substantially passes through extraction of the juice, peace and quiet, evaporation, crystallization, purging and the processing step of drying.And colour is always to weigh white One important indicator of granulated sugar quality, the white granulated sugar of current China makes what is be mainly made by sulfurous method, but It is that purification effect is relatively undesirable, considerable pigment is remained in syrup, causes the white granulated sugar colour being eventually fabricated higher, color Exceeded value is also an intractable problem present in sugar refining technology always.
The content of the invention
It is an object of the invention to:For problems of the prior art the white of white granulated sugar colour is reduced there is provided a kind of Granulated sugar production method, white granulated sugar colour is reduced by sugarcane selection, sugar refining technology efficiency.
To achieve these goals, the technical solution adopted by the present invention is:
It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour, comprise the following steps:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and gained sugar-cane juice is crossed into 80~200 mesh sieves, Normal juice and sieving residue after being sieved;By Normal juice after sieve be adjusted in advance pH6~ 6.5, be heated to 55~65 DEG C, be then added to neutralization reaction in stove drying averager, after reaction add milk of lime regulation pH11~ 11.5,90~100 DEG C are heated to, adds after flocculant and enters settler sedimentation, obtain supernatant juice and mud juice, mud juice is passed through into filter Filtered juice is obtained after cloth, through evaporating, adding SO again after supernatant juice and filtered juice are mixed2, crystallization and purification, dressing sieve crystal grain, dry it is brilliant Grain, by dried crystal grain by classifying except iron, packing, obtains white granulated sugar;
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant;
The settler includes tank body, and tank body includes cylinder portion and the cone portion positioned at cylinder subordinate end, institute It is provided with the inside of the upper end in the cylinder portion stated along the inwall of tank body and enters main loop groove around what is set, is entered main loop groove and be connected with into juice Pipe, the bottom for entering main loop groove is provided with the water conservancy diversion ring flat-plate set along the inwall and horizontal interior wall of tank body, the bottom of water conservancy diversion ring flat-plate In the cone portion for extending to tank body, water conservancy diversion ring flat-plate is used to the syrup entered in main loop groove being incorporated into tank base;Water conservancy diversion It is provided with above first order herringbone stabilier, first order herringbone stabilier side bead and also sets up above the end of ring flat-plate Have to be provided with above at least two second level herringbone stabiliers, second level herringbone stabilier and separate water conservancy diversion ring flat-plate inner chamber Juice yield tube is provided with above the current stabilization web plate opened, current stabilization web plate;Tank base is connected with mud juice discharge pipe.
Preferably, the head and afterbody that described sugarcane cuts are used for brown sugar and make raw material.
Preferably, described cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with compound Incorporation time is 5~10min during preparation.
By adopting the above-described technical solution, the beneficial effects of the invention are as follows:
The white granulated sugar production method of the reduction white granulated sugar colour of the present invention, removes head in sugarcane selection with afterbody containing sugar Amount is low, containing miscellaneous high part, the content of ammonia nitrogen effectively in reduction sugarcane raw material;The sedimentation higher by being provided with settling efficiency Device, so that stability contorting clarification process, improves the removal of nitrogen substance in clarifying process, reduces amino nitrogen content, final to improve The sugaring efficiency of whole sugar refining technology, it is to avoid contact iron container for a long time during sugaring and cause increasing for iron-holder, The colour of final effectively reduction white granulated sugar.
Brief description of the drawings
Fig. 1 is the structure diagram of the settler of the present invention.
Reference:1- tank bodies, 101- cylinders portion, 102- cones portion, 2- enters main loop groove, 3- juice yield tubes, 4- water conservancy diversion Ring flat-plate, 5- mud juice discharge pipes, 6- first order herringbone stabiliers, 7- second level herringbone stabilier, 8- current stabilization web plates, 9- enters Juice pipe.
Embodiment
A kind of white granulated sugar production method of reduction white granulated sugar colour of the present invention, comprises the following steps:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and the head and afterbody that sugarcane cuts are used for brown sugar and make raw material.Gained sugar-cane juice is crossed into 80~200 mesh sieves, obtained Normal juice and sieving residue after to sieve;Normal juice after sieve is adjusted to pH6~6.5 in advance, 55~65 DEG C is heated to, is then added in stove drying With neutralization reaction in device, milk of lime regulation pH11~11.5 are added after reaction, 90~100 DEG C is heated to, adds flocculant laggard Enter settler sedimentation, obtain supernatant juice and mud juice, by mud juice by obtaining filtered juice after filter cloth, supernatant juice and filtered juice are mixed By evaporation, add SO2, crystallization and purification, dressing sieve crystal grain, dry crystal grain again, by dried crystal grain by classifying except iron, packing, Obtain white granulated sugar.
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant.Cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with Incorporation time is 5~10min during compound formulation.
Reference picture 1, settler includes tank body 1, and tank body 1 includes cylinder portion 101 and positioned at the lower end of cylinder portion 101 Cone portion 102, be provided with the inside of the upper end in described cylinder portion 101 along the inwall of tank body 1 and to enter main loop around what is set Groove 2, enters main loop groove 2 and is connected with juice-feeding tube 9, and the bottom for entering main loop groove 2 is provided with what is set along the inwall and horizontal interior wall of tank body 1 Water conservancy diversion ring flat-plate 4, the bottom of water conservancy diversion ring flat-plate 4 is extended in the cone portion 102 of tank body 1, and water conservancy diversion ring flat-plate 4 is used to that juice will to be entered Syrup in annular groove 2 is incorporated into the bottom of tank body 1;First order herringbone stabilier 6 is provided with above the end of water conservancy diversion ring flat-plate 4, the At least two second level herringbone stabiliers 7, second level herringbone are additionally provided with above the side bead of one-level herringbone stabilier 6 The top of shape stabilier 7 is provided with the current stabilization web plate 8 for separating the inner chamber of water conservancy diversion ring flat-plate 4, and the top of current stabilization web plate 8 is provided with juice Pipe 3;The bottom of tank body 1 is connected with mud juice discharge pipe 5.
The present invention juice decanters, it is necessary to sedimentation syrup entered by juice-feeding tube 9 into main loop groove 2, Ran Houzai The bottom of tank body 1 is entered by entering the water conservancy diversion ring flat-plate 4 of the bottom of main loop groove 2, enters the use of main loop groove 2 and water conservancy diversion ring flat-plate 44 and is close to The inwall of tank body 1 is set, and syrup finally slowly drops into the bottom of tank body 1, enters subsidence stage.Even if the syrup newly entered Can have an impact to the juice mud of the bottom of tank body 1, first order herringbone stabilier 6, the and of second level herringbone stabilier 7 can also be passed through The current stabilization effect of current stabilization web plate 8, it is ensured that the clear liquid on current stabilization web plate 8 will not be affected.
With reference to specific embodiment, the manufacturing process of the white granulated sugar of the present invention is illustrated.
Embodiment 1:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and the head and afterbody that sugarcane cuts are used for brown sugar and make raw material.Gained sugar-cane juice is crossed into 200 mesh sieves, sieved Normal juice and sieving residue afterwards;Normal juice after sieve is adjusted to pH6.2 in advance, 65 DEG C are heated to, is then added in stove drying averager and neutralizes Reaction, adds milk of lime regulation pH11.5, is heated to 100 DEG C, add after flocculant and enter settler sedimentation, obtain after reaction Supernatant juice and mud juice, by mud juice by obtaining filtered juice after filter cloth, will supernatant juice and filtered juice mix after through evaporation, again plus SO2, Crystallization and purification, dressing sieve crystal grain, dry crystal grain, by dried crystal grain by classifying except iron, packing, obtain white granulated sugar.
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant.Cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with Incorporation time is 6min during compound formulation.
Embodiment 2:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and the head and afterbody that sugarcane cuts are used for brown sugar and make raw material.Gained sugar-cane juice is crossed into 80 mesh sieves, obtained after sieve Normal juice and sieving residue;Normal juice after sieve is adjusted to pH6 in advance, 65 DEG C are heated to, neutralization reaction in stove drying averager is then added to, Milk of lime regulation pH11 is added after reaction, 100 DEG C are heated to, adds after flocculant and enters settler sedimentation, obtain supernatant juice and Mud juice, by mud juice by obtaining filtered juice after filter cloth, adds SO2, crystallization to carry after supernatant juice and filtered juice are mixed through evaporation, again Pure, dressing sieve crystal grain, dry crystal grain, by dried crystal grain by classifying except iron, packing, obtain white granulated sugar.
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant.Cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with Incorporation time is 10min during compound formulation.
Embodiment 3:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and the head and afterbody that sugarcane cuts are used for brown sugar and make raw material.Gained sugar-cane juice is crossed into 100 mesh sieves, sieved Normal juice and sieving residue afterwards;Normal juice after sieve is adjusted to pH6.5 in advance, 55 DEG C are heated to, is then added in stove drying averager and neutralizes Reaction, adds milk of lime regulation pH11, is heated to 90 DEG C, add after flocculant and enter settler sedimentation, obtain supernatant after reaction Juice and mud juice, by mud juice by obtaining filtered juice after filter cloth, add SO2, crystallization through evaporation, again after supernatant juice and filtered juice are mixed Purification, dressing sieve crystal grain, dry crystal grain, by dried crystal grain by classifying except iron, packing, obtain white granulated sugar.
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant.Cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with Incorporation time is 5min during compound formulation.
Embodiment 4:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and the head and afterbody that sugarcane cuts are used for brown sugar and make raw material.Gained sugar-cane juice is crossed into 80~200 mesh sieves, obtained Normal juice and sieving residue after to sieve;Normal juice after sieve is adjusted to pH6 in advance, 62 DEG C are heated to, in being then added in stove drying averager And reaction, milk of lime regulation pH11.2 is added after reaction, 95 DEG C are heated to, adds after flocculant and enters settler sedimentation, obtain Supernatant juice and mud juice, by mud juice by obtaining filtered juice after filter cloth, will supernatant juice and filtered juice mix after through evaporation, again plus SO2, Crystallization and purification, dressing sieve crystal grain, dry crystal grain, by dried crystal grain by classifying except iron, packing, obtain white granulated sugar.
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant.Cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with Incorporation time is 6min during compound formulation.
Embodiment 5:
The head of sugarcane is cut carried out after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length it is sweet Sugarcane is squeezed the juice, and the head and afterbody that sugarcane cuts are used for brown sugar and make raw material.Gained sugar-cane juice is crossed into 80 mesh sieves, obtained after sieve Normal juice and sieving residue;Normal juice after sieve is adjusted to pH6.5 in advance, 58 DEG C are heated to, is then added in stove drying averager and neutralizes instead Should, milk of lime regulation pH11 is added after reaction, 98 DEG C are heated to, adds after flocculant and enters settler sedimentation, obtain supernatant juice And mud juice, by mud juice by obtaining filtered juice after filter cloth, add SO2, crystallization to carry through evaporation, again after supernatant juice and filtered juice are mixed Pure, dressing sieve crystal grain, dry crystal grain, by dried crystal grain by classifying except iron, packing, obtain white granulated sugar.
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It is poly- It is 1 to close aluminium chloride:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1:120 ratio is mixed into flocculant.Cationic polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with Incorporation time is 8min during compound formulation.
The one-level white granulated sugar made according to embodiment 1-5 technique is obtained, by determining the pigment content of white sugar sample, is obtained To the colour of white granulated sugar, as shown in table 1.
The white granulated sugar pigment content of table 1
By said determination result, the colour content of white granulated sugar is relative to common production technology or existing production work For skill, hence it is evident that reduction.

Claims (3)

1. a kind of reduce the white granulated sugar production method of white granulated sugar colour, it is characterised in that comprises the following steps:
The head of sugarcane is cut after the 1/8 of the sugarcane total length, afterbody of sugarcane cuts the 1/6 of sugarcane total length and carries out sugarcane squeezing Juice, 80~200 mesh sieves are crossed by gained sugar-cane juice, Normal juice and sieving residue after being sieved;Normal juice after sieve is adjusted to pH6~6.5 in advance, 55~65 DEG C are heated to, neutralization reaction in stove drying averager is then added to, milk of lime regulation pH11~11.5 are added after reaction, Be heated to 90~100 DEG C, add after flocculant and enter settler sedimentation, obtain supernatant juice and mud juice, by mud juice by filter cloth after Filtered juice is obtained, through evaporating, adding SO again after supernatant juice and filtered juice are mixed2, crystallization and purification, dressing sieve crystal grain, dry crystal grain, will Dried crystal grain obtains white granulated sugar by classifying except iron, packing;
The preparation method of the flocculant:Raw material cationic polyacrylic acid by volume:Anionic polypropylene amine:It polymerize chlorine It is 1 to change aluminium:1:1.5 ratio is mixed to form compound formulation, then will meet preparation according to volume ratio compound formulation:Water is 1: 120 ratio is mixed into flocculant;
The settler includes tank body, and tank body includes cylinder portion and the cone portion positioned at cylinder subordinate end, described It is provided with the inside of the upper end in cylinder portion along the inwall of tank body and enters main loop groove around what is set, is entered main loop groove and be connected with juice-feeding tube, The bottom for entering main loop groove is provided with the water conservancy diversion ring flat-plate set along the inwall and horizontal interior wall of tank body, and the bottom of water conservancy diversion ring flat-plate is always In the cone portion for extending to tank body, water conservancy diversion ring flat-plate is used to the syrup entered in main loop groove being incorporated into tank base;Water conservancy diversion ring flat-plate End above be provided with above first order herringbone stabilier, first order herringbone stabilier side bead be additionally provided with to It is provided with separate water conservancy diversion ring flat-plate inner chamber above few two second level herringbone stabiliers, second level herringbone stabilier Juice yield tube is provided with above current stabilization web plate, current stabilization web plate;Tank base is connected with mud juice discharge pipe.
2. the white granulated sugar production method of reduction white granulated sugar colour according to claim 1, it is characterised in that described sugarcane The head cut and afterbody are used for brown sugar and make raw material.
3. the white granulated sugar production method of reduction white granulated sugar colour according to claim 1, it is characterised in that described sun from Incorporation time is 5~10min when subtype polyacrylic acid, anionic polypropylene amine, aluminium polychloride are mixed with compound formulation.
CN201710359930.XA 2017-05-20 2017-05-20 It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour Pending CN107164569A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710359930.XA CN107164569A (en) 2017-05-20 2017-05-20 It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710359930.XA CN107164569A (en) 2017-05-20 2017-05-20 It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour

Publications (1)

Publication Number Publication Date
CN107164569A true CN107164569A (en) 2017-09-15

Family

ID=59816195

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710359930.XA Pending CN107164569A (en) 2017-05-20 2017-05-20 It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour

Country Status (1)

Country Link
CN (1) CN107164569A (en)

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB645192A (en) * 1946-10-12 1950-10-25 American Cyanamid Co Improvements in or relating to the purification of aqueous solutions of sugar
CN201128742Y (en) * 2007-01-31 2008-10-08 黄桂忠 Static fast settling vessel
CN103114155A (en) * 2012-11-30 2013-05-22 南宁苏格尔科技有限公司 Method for settling extracted sugarcane juice by using weak base
CN203315808U (en) * 2013-02-01 2013-12-04 南宁苏格尔科技有限公司 Rapid single-layer settler
CN203498393U (en) * 2013-07-09 2014-03-26 河南工业大学 Rapid settler for sugar juice
CN103981290A (en) * 2014-05-30 2014-08-13 彭华成 Process for preparing sugar from cane
CN104357587A (en) * 2014-11-24 2015-02-18 临沧南华糖业有限公司 Carbon-sulfur combining sugar juice carbonation and clarifying method through CO2 generated from alcohol in production of sugar from sugarcane
CN104388600A (en) * 2014-10-21 2015-03-04 南宁苏格尔科技有限公司 Sugar manufacturing technique for improving yield and reducing color value of white sugar

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB645192A (en) * 1946-10-12 1950-10-25 American Cyanamid Co Improvements in or relating to the purification of aqueous solutions of sugar
CN201128742Y (en) * 2007-01-31 2008-10-08 黄桂忠 Static fast settling vessel
CN103114155A (en) * 2012-11-30 2013-05-22 南宁苏格尔科技有限公司 Method for settling extracted sugarcane juice by using weak base
CN203315808U (en) * 2013-02-01 2013-12-04 南宁苏格尔科技有限公司 Rapid single-layer settler
CN203498393U (en) * 2013-07-09 2014-03-26 河南工业大学 Rapid settler for sugar juice
CN103981290A (en) * 2014-05-30 2014-08-13 彭华成 Process for preparing sugar from cane
CN104388600A (en) * 2014-10-21 2015-03-04 南宁苏格尔科技有限公司 Sugar manufacturing technique for improving yield and reducing color value of white sugar
CN104357587A (en) * 2014-11-24 2015-02-18 临沧南华糖业有限公司 Carbon-sulfur combining sugar juice carbonation and clarifying method through CO2 generated from alcohol in production of sugar from sugarcane

Similar Documents

Publication Publication Date Title
CN101225448B (en) Technology of carbonation process sugar factory for reducing and eliminating solid waste discharge and changing them into useful materials
JP3436540B2 (en) Sugar beet juice purification method
CN105002306B (en) A kind of syrup is without sulfur highly effective purification method
CN103114155B (en) Method for settling extracted sugarcane juice by using weak base
CN105154591A (en) Production method of sugar cane juice brown sugar powder
DE102006004103A1 (en) Method for cleaning raw sugar-beet juice, comprises preliming the raw juice, first main-liming the prelimed raw juice, and clarifying the pre-limed raw juice after the main-liming in a separation device
CN105063241A (en) Sulfitation syrup floatation clarification process
CN107986952A (en) A kind of continuous crystallisation process of purifying vanillin
CN102351245A (en) Continuous production method for ammonium vanadate
WO2005042787A1 (en) Method for reducing the lime consumption during sugar-beet juice cleaning
CN107164569A (en) It is a kind of to reduce the white granulated sugar production method of white granulated sugar colour
KR101116926B1 (en) Method for white sucrose, brown sucrose and black sucrose production using direct recovery process
CN103710467B (en) Process for making sugar by using sorgo
US11679371B2 (en) Method for producing functionally improved carbolime
CN102978296A (en) Method for cleaning refractory cane juice for sugar factories by using sulfurous method
CN104071809A (en) Production method for food-grade potassium metabisulfite
CN114540553A (en) Production method of sugarcane sulfur-free white granulated sugar
CN103060479B (en) Method for cleaning sugar preparing and boiling materials
CN104357587A (en) Carbon-sulfur combining sugar juice carbonation and clarifying method through CO2 generated from alcohol in production of sugar from sugarcane
CN206706130U (en) A kind of juice decanters
CN107760804A (en) A kind of processing method of embrane method processing sugar-cane juice trapped fluid
CN106119428A (en) A kind of brown sugar (Saccharum Sinensis Roxb.) remelt syrup two step method clarification process
CN108315501A (en) A kind of cane sugar manufacture clarifies new process without sulphur
CN113462822B (en) Sugar production process based on membrane method clarification poly-generation
US270042A (en) Office

Legal Events

Date Code Title Description
PB01 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: 20170915

RJ01 Rejection of invention patent application after publication