CN204690018U - A kind of processing unit (plant) of ecosystem brown sugar - Google Patents
A kind of processing unit (plant) of ecosystem brown sugar Download PDFInfo
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- CN204690018U CN204690018U CN201520197640.6U CN201520197640U CN204690018U CN 204690018 U CN204690018 U CN 204690018U CN 201520197640 U CN201520197640 U CN 201520197640U CN 204690018 U CN204690018 U CN 204690018U
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Abstract
A processing unit (plant) for ecosystem brown sugar, includes the squeezing coarse filtration equipment, interchanger, multistage ceramic membrane ultrafitration equipment, falling film type triple effect vacuum vaporation system, Water Jet Condenser, interlayer iron pan and the graining dry forming equipment that connect successively.Clarified sugar cane juice case is connected with between described multistage ceramic membrane ultrafitration equipment and triple effect vacuum-evaporation appts; Syrup case is connected with between described falling film type triple effect vacuum vaporation system and interlayer iron pan.The brown sugar crystal grain utilizing device described in the utility model obtained is tiny, in brown to Vandyke brown, and natural in color, impure less, natural caramel charcoal is had to burn joss sticks, fragrant liquor-saturated strong, sweet pleasant, delicate mouthfeel, preserves nutritious sugarcane composition to greatest extent, has very high nutritive value; After being dissolved to 11.5 ° of Bx, turbidity is at below 0.5NTU, solves the phenomenon having black slag after brown sugar dissolves, improves the quality of brown sugar.
Description
Technical field
The utility model relates to a kind of processing unit (plant) of ecosystem brown sugar, belongs to food machinery field.
Technical background
Sugarcane is the distinctive a kind of fruit in subtropics, and its juice enriches, and sugar degree is high, and sense of taste is fresh and sweet, and also containing the trace element such as calcium, potassium, iron, magnesium and folic acid and other mineral substance, nutritive value is very high, is beneficial to acid base equilibrium in human body, is widely loved by the people.Brown sugar original idea is color darker, do not pass through height refining edible sucrose, it remains sugarcane major part effectively nutritive ingredient.Brown sugar on domestic market mainly based on import Japan and TaiWan, China, domesticly yet there are no relevant product Report.Guangxi is the sugarcane place of production, utilizes the resource of advantage, and exploitation brown sugar product is one of Guangxi sugar-refining industry product diversification countermeasure.
Traditional brown sugar complete processing is heated being poured in pot by sugar cane juice after sugar cane crushing, boil rear cane juice impurities can float up, impurity is filtered, and then heating evaporation is concentrated to a certain degree and pours rapidly smooth desktop into, can brown sugar be obtained after cooling in several minutes.This kind of complete processing gained brown sugar is impure more, and due to its cane juice impurities floating after sugar cane juice boils, impurity filters by side, more sugar cane juice will inevitably be wasted, take away part nutritive ingredient, in addition this kind of process industry level is low, consumes energy high, reduces the production efficiency of brown sugar to a great extent.And the sugar cane juice clarification means of modern brown sugar processing unit (plant) are divided into two kinds, i.e. sulfurous method and carbonatation process.This two method also can remove nutritive ingredients a large amount of in sugar cane juice when reaching clarifying effect, reduces the quality of brown sugar to a great extent.
" People's Republic of China (PRC) light industry standard QB/T 4567-2013 " about brown sugar standard formally performed on July 1st, 2014, its clear stipulaties brown sugar quality standard, wherein clear stipulaties (seeing the following form) is carried out to the sense organ of brown sugar, brown sugar that traditional technology is produced is impure higher, therefore needs to improve it.
Brown sugar organoleptic requirements
Utility model content
The purpose of this utility model is to provide a kind of processing unit (plant) of ecosystem brown sugar, to improve industrialized level and the quality of brown sugar.
To achieve these goals, the utility model have employed following technical scheme,
A processing unit (plant) for ecosystem brown sugar, includes the squeezing coarse filtration equipment, interchanger, multistage ceramic membrane ultrafitration equipment, falling film type triple effect vacuum vaporation system, Water Jet Condenser, interlayer iron pan and the graining dry forming equipment that connect successively.
Clarified sugar cane juice case is connected with between described multistage ceramic membrane ultrafitration equipment and triple effect vacuum-evaporation appts;
Syrup case is connected with between described falling film type triple effect vacuum vaporation system and interlayer iron pan;
Described falling film type triple effect vacuum vaporation system comprises that falling film type one imitates vacuum evaporating pot, falling film type two imitates vacuum evaporating pot and falling film type triple effect vacuum evaporating pot.
Concrete mode of connection is as follows:
The outlet of coarse filtration sugar cane juice bin is connected with the material inlet of interchanger, the material outlet of interchanger is connected with the juice mouth that enters of multistage ceramic membrane ultrafitration equipment, the concentrated solution outlet of multistage ceramic membrane ultrafitration equipment is connected to concentrated solution bin, and the permeate outlet of multistage ceramic membrane ultrafitration equipment is connected to clarified sugar cane juice case; Outlet and the falling film type one of clarified sugar cane juice case are imitated vacuum evaporating pot and are entered juice mouth and be connected; Falling film type one is imitated vacuum evaporating pot juice opening and is imitated vacuum evaporating pot with falling film type two by Y-tube simultaneously and enter juice mouth and falling film type one and imitate vacuum evaporating pot and circulate into juice mouth and be connected; Falling film type two is imitated vacuum evaporating pot juice opening and is entered juice mouth and falling film type two with falling film type triple effect vacuum evaporating pot by Y-tube simultaneously and imitate vacuum evaporating pot and circulate into juice mouth and be connected; Falling film type triple effect vacuum evaporating pot juice opening is circulated into juice mouth with syrup case and falling film type triple effect vacuum evaporating pot by Y-tube simultaneously and is connected; The outlet of syrup case is connected to interlayer iron pan heavy syrup entrance, and interlayer iron pan boils massecuite outlet and is connected to graining dry forming equipment;
Falling film type one is imitated vacuum evaporating pot heating steam inlet and is connected with heating steam source; Falling film type one is imitated the outlet of vacuum evaporating pot secondary steam and is imitated vacuum evaporating pot heating steam inlet with falling film type two and be connected; Falling film type two is imitated the outlet of vacuum evaporating pot secondary steam and is connected with falling film type triple effect vacuum evaporating pot heating steam inlet; The outlet of falling film type triple effect vacuum evaporating pot secondary steam connects with Water Jet Condenser; Falling film type one imitates that vacuum evaporating pot vapour coagulates water out, falling film type two is imitated vacuum evaporating pot vapour and coagulated water out and falling film type triple effect vacuum evaporating pot vapour and coagulate water out and be connected to vapour and coagulate water pot;
Interlayer iron pan heating steam entrance is connected with heating steam source, and interlayer iron pan vapour coagulates water out and is connected to vapour and coagulates water pot;
The heating steam entrance of interchanger is connected with heating steam source, and the vapour of interchanger coagulates water out and is connected to vapour and coagulates water pot.
Described squeezing coarse filtration equipment includes the shredder, squeezing machine, hollander, horizontal centrifuge and the coarse filtration sugar cane juice bin that connect successively.
Described graining dry forming equipment includes the crystallization in motion case connected successively, wood mold coupled and wrapping machine.
Described multistage ceramic membrane ultrafitration equipment is the ceramic super-filtering film of Pyatyi parallel connection, and every grade of ceramic membrane is made up of two membrane modules, wherein has one-level to play wheel and washes replacing effect, and the membrane pore size of ceramic super-filtering film is 0.02 ~ 0.10 μm.
Compared with prior art, the beneficial effect that possesses of the utility model:
The utility model solves brown sugar and filters in process of production and clear up problems, effectively can remove the impurity of 50 ~ 1400nm, ensure the clean inclusion-free of syrup, solve brown sugar for a long time and occur sedimentary problem after dissolving, retain the effective nutritious material of sugarcane simultaneously; Have employed ceramic membrane ultrafitration clarification in sugar cane juice clarification process, clarifying effect is better; And the membrane resistance that on ceramic membrane, fouling causes is less, therefore the membrane permeation flux of ceramic membrane filter sugar cane juice is comparatively large, and the pottery membrane flux rate of decay is slow, can maintain higher membrane flux and filter, thus extend the Membrane cleaning cycle and reduce cleaning frequency membrane.
The utility model is that one can industrialization continuous seepage, solves traditional brown sugar and produces manual numerous and diverse.
The utility model utilizes interlayer iron pan to stir off, and solves brown sugar and boils the shallow problem of product colour and bring enough iron ions into, benefit people and enrich blood.
The utility model does not add any chemical reagent and foodstuff additive in the ecosystem brown sugar course of processing, ensure that the green safety of food.
The utility model adopts vacuum vaporation system and interlayer iron pan to instead of traditional a chain of pot sugar cook evaporation, and industrialized level is high, and energy consumption is low, and production efficiency is large.
Brown sugar crystal grain obtained by the utility model is tiny, in brown to Vandyke brown, and natural in color, impure less, have natural caramel charcoal to burn joss sticks, fragrant liquor-saturated strong, sweet pleasant, delicate mouthfeel, preserves nutritious sugarcane composition to greatest extent, has very high nutritive value; After being dissolved to 11.5 ° of Bx, turbidity is at below 0.5NTU, solves the phenomenon having black slag after brown sugar dissolves, improves the quality of brown sugar.
Accompanying drawing explanation
The processing unit (plant) schematic diagram of the ecosystem brown sugar that Fig. 1 provides for the utility model.
Fig. 2 is multistage ceramic membrane ultrafitration equipment schematic diagram described in the utility model.
In figure: 1-hollander; 2-horizontal centrifuge; 3-coarse filtration sugar cane juice bin; 4-interchanger; 5-multistage ceramic membrane ultrafitration equipment; 6-clarified sugar cane juice case; 7-falling film type one is imitated vacuum evaporating pot and is entered juice mouth; 8-falling film type one is imitated vacuum evaporating pot and is circulated into juice mouth; 9-falling film type one imitates vacuum evaporating pot heating steam inlet; 10-falling film type two is imitated vacuum evaporating pot and is entered juice mouth; 11-falling film type two is imitated vacuum evaporating pot and is circulated into juice mouth; 12-falling film type two imitates vacuum evaporating pot heating steam inlet; 13-falling film type triple effect vacuum evaporating pot enters juice mouth; 14-falling film type triple effect vacuum evaporating pot circulates into juice mouth; 15-falling film type triple effect vacuum evaporating pot heating steam inlet; 16-graining dry forming equipment; 17-Water Jet Condenser; 18-interlayer iron pan; 19-syrup case; 20-falling film type triple effect vacuum evaporating pot juice opening; 21-falling film type triple effect vacuum evaporating pot; 22-falling film type triple effect vacuum evaporating pot secondary steam exports; 23-falling film type two imitates vacuum evaporating pot; 24-falling film type two imitates vacuum evaporating pot juice opening; 25-falling film type two imitates the outlet of vacuum evaporating pot secondary steam; 26-falling film type one imitates vacuum evaporating pot juice opening; 27-falling film type one imitates vacuum evaporating pot; 28-falling film type one imitates the outlet of vacuum evaporating pot secondary steam; 29-multistage ceramic membrane equipment concentrated solution outlet; 31-shredder; 32-squeezing machine; Falling film type triple effect vacuum evaporating pot vapour coagulates water out 33; Falling film type two is imitated vacuum evaporating pot vapour and is coagulated water out 34; Falling film type one is imitated vacuum evaporating pot vapour and is coagulated water out 35; 181-interlayer iron pan heating steam entrance; 182-interlayer iron pan boils massecuite outlet; 183-interlayer iron pan vapour coagulates water out; 184-interlayer iron pan noncondensable gas exports; 185-interlayer iron pan heavy syrup entrance.
Embodiment
Embodiment 1
A processing unit (plant) for ecosystem brown sugar, includes the squeezing coarse filtration equipment, interchanger 4, multistage ceramic membrane ultrafitration equipment 5, falling film type triple effect vacuum vaporation system, Water Jet Condenser 17, interlayer iron pan 18 and the graining dry forming equipment that connect successively.
Clarified sugar cane juice case 6 is connected with between described multistage ceramic membrane ultrafitration equipment 5 and triple effect vacuum-evaporation appts;
Syrup case 19 is connected with between described falling film type triple effect vacuum vaporation system and interlayer iron pan;
Described falling film type triple effect vacuum vaporation system comprises that falling film type one imitates vacuum evaporating pot 27, falling film type two imitates vacuum evaporating pot 23 and falling film type triple effect vacuum evaporating pot 21.
Concrete mode of connection is as follows:
The outlet of coarse filtration sugar cane juice bin 3 is connected with the material inlet of interchanger 4, the material outlet of interchanger 4 is connected with the juice mouth that enters of multistage ceramic membrane ultrafitration equipment 5, the concentrated solution outlet of multistage ceramic membrane ultrafitration equipment 5 is connected to concentrated solution bin, and the permeate outlet of multistage ceramic membrane ultrafitration equipment 5 is connected to clarified sugar cane juice case 6; Outlet and the falling film type one of clarified sugar cane juice case 6 are imitated vacuum evaporating pot and are entered juice mouth 7 and be connected; Falling film type one is imitated vacuum evaporating pot juice opening 26 and is imitated vacuum evaporating pot with falling film type two by Y-tube simultaneously and enter juice mouth 10 and falling film type one and imitate vacuum evaporating pot and circulate into juice mouth 8 and be connected; Falling film type two is imitated vacuum evaporating pot juice opening 24 and is entered juice mouth 13 and falling film type two with falling film type triple effect vacuum evaporating pot by Y-tube simultaneously and imitate vacuum evaporating pot and circulate into juice mouth 14 and be connected; Falling film type triple effect vacuum evaporating pot juice opening 20 is circulated into juice mouth 14 with syrup case 19 and falling film type triple effect vacuum evaporating pot by Y-tube simultaneously and is connected; The outlet of syrup case 19 is connected to interlayer iron pan heavy syrup entrance 185, and interlayer iron pan boils massecuite outlet 182 and is connected to graining dry forming equipment;
Falling film type one is imitated vacuum evaporating pot heating steam inlet 9 and is connected with heating steam source; Falling film type one is imitated vacuum evaporating pot secondary steam outlet 28 and is imitated vacuum evaporating pot heating steam inlet 12 with falling film type two and be connected; Falling film type two is imitated vacuum evaporating pot secondary steam outlet 25 and is connected with falling film type triple effect vacuum evaporating pot heating steam inlet 15; Falling film type triple effect vacuum evaporating pot secondary steam outlet 22 connects with Water Jet Condenser 17; Falling film type one imitates that vacuum evaporating pot vapour coagulates water out 35, falling film type two is imitated vacuum evaporating pot vapour and coagulated water out 34 and falling film type triple effect vacuum evaporating pot vapour and coagulate water out 33 and be connected to vapour and coagulate water pot;
Interlayer iron pan heating steam entrance 181 is connected with heating steam source, and interlayer iron pan vapour coagulates water out 183 and is connected to vapour and coagulates water pot;
The heating steam entrance of interchanger 4 is connected with heating steam source, and the vapour of interchanger 4 coagulates water out and is connected to vapour and coagulates water pot.
Described squeezing coarse filtration equipment includes the shredder 31, squeezing machine 32, hollander 1, horizontal centrifuge 2 and the coarse filtration sugar cane juice bin 3 that connect successively;
Described graining dry forming equipment includes the crystallization in motion case connected successively, wood mold coupled and wrapping machine.
Described multistage ceramic membrane ultrafitration equipment 5 is the ceramic super-filtering film of Pyatyi parallel connection, and every grade of ceramic membrane is made up of two membrane modules, wherein has one-level to play wheel and washes replacing effect, and the membrane pore size of ceramic super-filtering film is 0.02 ~ 0.10 μm.
Embodiment 2
The present embodiment is the specific examples utilizing the processing unit (plant) of ecosystem brown sugar described in the utility model to carry out producing, and concrete operation step is:
(1) squeeze juice extracting coarse filtration: sugarcane is sent into after shredder tears the sugarcane material such as solution becomes thread, sheet, strip, send into three-roller type squeezing machine squeeze juice extracting, in order to improve crushing juice rate, the bagasse obtained after can squeezing the juice toward first time sprays a small amount of water, squeeze the juice again, obtain sugar cane juice for subsequent use; Be first that the making beating of 0.1mm pulp grinder is filtered through punching footpath by sugar cane juice, then be that 400 object horizontal centrifuges filter further through mesh size, thus the large granular impurity such as sugarcane chaff, sugarcane bits in removing sugar cane juice, obtain coarse filtration sugar cane juice for subsequent use;
(2) heat: with interlayer iron pan, coarse filtration sugar cane juice is heated to 100 DEG C, keep 1min, thus reduce the viscosity of sugar cane juice, be convenient to filter, obtain heating sugar cane juice for subsequent use;
(3) ceramic membrane ultrafitration clarification: heating sugar cane juice is sent into multistage ceramic membrane ultrafitration equipment, ultra filtering clarifying is carried out with the ceramic super-filtering film that aperture is 0.10 μm, the operational condition of ceramic membrane ultrafitration is: transmembrane pressure is 0.30MPa, filtration temperature is 70 DEG C, crossflow velocity is 5m/s, and obtaining turbidity, to be less than 0.5NTU sugarcane subsider juice for subsequent use;
(4) vacuum concentration: sugarcane subsider juice is sent into falling film type vacuum vaporation system, and by its evaporation concentration to 50 ° Bx, obtains heavy syrup for subsequent use;
(5) stir off: at ambient pressure, utilize interlayer iron pan, keep heavy syrup to concentrate further at the temperature of 120 ~ 125 DEG C, obtain 86 ° of Bx and boil massecuite;
(6) sanding is shaping: will boil massecuite and move in crystallization in motion case, stir to pour out after graining be covered with through strict sterilization sterilization food paper using wood mold coupled in, make its naturally cooling shaping, then be packaged to be ecosystem brown sugar after removing paper.
Technic index in embodiment 2 production process is as shown in the table:
Embodiment 3
The present embodiment is utilize the processing unit (plant) of ecosystem brown sugar described in the utility model to carry out another specific examples produced, and concrete operation step is:
(1) squeeze juice extracting coarse filtration: sugarcane is sent into after shredder tears the sugarcane material such as solution becomes thread, sheet, strip, send into three-roller type squeezing machine squeeze juice extracting, in order to improve crushing juice rate, the bagasse obtained after can squeezing the juice toward first time sprays a small amount of water, squeeze the juice again, obtain sugar cane juice for subsequent use; Be first that the making beating of 0.1mm pulp grinder is filtered through punching footpath by sugar cane juice, then be that 400 object horizontal centrifuges filter further through mesh size, thus the large granular impurity such as sugarcane chaff, sugarcane bits in removing sugar cane juice, obtain coarse filtration sugar cane juice for subsequent use;
(2) heat: with interlayer iron pan, coarse filtration sugar cane juice is heated to 90 DEG C, keep 3min, thus reduce the viscosity of sugar cane juice, be convenient to filter, obtain heating sugar cane juice for subsequent use;
(3) ceramic membrane ultrafitration clarification: heating sugar cane juice is sent into multistage ceramic membrane ultrafitration equipment, ultra filtering clarifying is carried out with the ceramic super-filtering film that aperture is 0.05 μm, the operational condition of ceramic membrane ultrafitration is: transmembrane pressure is 0.10MPa, filtration temperature is 90 DEG C, crossflow velocity is 4m/s, and obtaining turbidity, to be less than 0.5NTU sugarcane subsider juice for subsequent use;
(4) vacuum concentration: sugarcane subsider juice is sent into falling film type triple effect vacuum vaporation system, and by its evaporation concentration to 65 ° Bx, obtain heavy syrup for subsequent use;
(5) stir off: at ambient pressure, utilize interlayer iron pan, keep heavy syrup to concentrate further at the temperature of 120 ~ 125 DEG C, obtain 90 ° of Bx and boil massecuite;
(6) sanding is shaping: will boil massecuite and move in crystallization in motion case, stir to pour out after graining be covered with through strict sterilization sterilization food paper using wood mold coupled in, make its naturally cooling shaping, then be packaged to be ecosystem brown sugar after removing paper.
Technic index in embodiment 3 production process is as shown in the table:
Claims (6)
1. the processing unit (plant) of an ecosystem brown sugar, it is characterized in that, include the squeezing coarse filtration equipment, interchanger, multistage ceramic membrane ultrafitration equipment, falling film type triple effect vacuum vaporation system, Water Jet Condenser, interlayer iron pan and the graining dry forming equipment that connect successively.
2. the processing unit (plant) of ecosystem brown sugar as claimed in claim 1, is characterized in that,
Clarified sugar cane juice case is connected with between described multistage ceramic membrane ultrafitration equipment and triple effect vacuum-evaporation appts;
Syrup case is connected with between described falling film type triple effect vacuum vaporation system and interlayer iron pan;
Described falling film type triple effect vacuum vaporation system comprises that falling film type one imitates vacuum evaporating pot, falling film type two imitates vacuum evaporating pot and falling film type triple effect vacuum evaporating pot.
3. the processing unit (plant) of ecosystem brown sugar as claimed in claim 2, it is characterized in that, concrete mode of connection is as follows:
The outlet of coarse filtration sugar cane juice bin is connected with the material inlet of interchanger, the material outlet of interchanger is connected with the juice mouth that enters of multistage ceramic membrane ultrafitration equipment, the concentrated solution outlet of multistage ceramic membrane ultrafitration equipment is connected to concentrated solution bin, and the permeate outlet of multistage ceramic membrane ultrafitration equipment is connected to clarified sugar cane juice case; Outlet and the falling film type one of clarified sugar cane juice case are imitated vacuum evaporating pot and are entered juice mouth and be connected; Falling film type one is imitated vacuum evaporating pot juice opening and is imitated vacuum evaporating pot with falling film type two by Y-tube simultaneously and enter juice mouth and falling film type one and imitate vacuum evaporating pot and circulate into juice mouth and be connected; Falling film type two is imitated vacuum evaporating pot juice opening and is entered juice mouth and falling film type two with falling film type triple effect vacuum evaporating pot by Y-tube simultaneously and imitate vacuum evaporating pot and circulate into juice mouth and be connected; Falling film type triple effect vacuum evaporating pot juice opening is circulated into juice mouth with syrup case and falling film type triple effect vacuum evaporating pot by Y-tube simultaneously and is connected; The outlet of syrup case is connected to interlayer iron pan heavy syrup entrance, and interlayer iron pan boils massecuite outlet and is connected to graining dry forming equipment;
Falling film type one is imitated vacuum evaporating pot heating steam inlet and is connected with heating steam source; Falling film type one is imitated the outlet of vacuum evaporating pot secondary steam and is imitated vacuum evaporating pot heating steam inlet with falling film type two and be connected; Falling film type two is imitated the outlet of vacuum evaporating pot secondary steam and is connected with falling film type triple effect vacuum evaporating pot heating steam inlet; The outlet of falling film type triple effect vacuum evaporating pot secondary steam connects with Water Jet Condenser; Falling film type one imitates that vacuum evaporating pot vapour coagulates water out, falling film type two is imitated vacuum evaporating pot vapour and coagulated water out and falling film type triple effect vacuum evaporating pot vapour and coagulate water out and be connected to vapour and coagulate water pot;
Interlayer iron pan heating steam entrance is connected with heating steam source, and interlayer iron pan vapour coagulates water out and is connected to vapour and coagulates water pot;
The heating steam entrance of interchanger is connected with heating steam source, and the vapour of interchanger coagulates water out and is connected to vapour and coagulates water pot.
4. the processing unit (plant) of the ecosystem brown sugar as described in claims 1 to 3 any one, is characterized in that, described squeezing coarse filtration equipment includes the shredder, squeezing machine, hollander, horizontal centrifuge and the coarse filtration sugar cane juice bin that connect successively.
5. the processing unit (plant) of the ecosystem brown sugar as described in claims 1 to 3 any one, is characterized in that, described graining dry forming equipment includes the crystallization in motion case connected successively, wood mold coupled and wrapping machine.
6. the processing unit (plant) of the ecosystem brown sugar as described in claims 1 to 3 any one, it is characterized in that, described multistage ceramic membrane ultrafitration equipment is the ceramic super-filtering film of Pyatyi parallel connection, every grade of ceramic membrane is made up of two membrane modules, wherein have one-level to play wheel and wash replacing effect, the membrane pore size of ceramic super-filtering film is 0.02 ~ 0.10 μm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201520197640.6U CN204690018U (en) | 2015-04-02 | 2015-04-02 | A kind of processing unit (plant) of ecosystem brown sugar |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520197640.6U CN204690018U (en) | 2015-04-02 | 2015-04-02 | A kind of processing unit (plant) of ecosystem brown sugar |
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| CN204690018U true CN204690018U (en) | 2015-10-07 |
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| CN201520197640.6U Withdrawn - After Issue CN204690018U (en) | 2015-04-02 | 2015-04-02 | A kind of processing unit (plant) of ecosystem brown sugar |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104805224A (en) * | 2015-04-02 | 2015-07-29 | 广西大学 | Originally ecological black sugar processing device |
-
2015
- 2015-04-02 CN CN201520197640.6U patent/CN204690018U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104805224A (en) * | 2015-04-02 | 2015-07-29 | 广西大学 | Originally ecological black sugar processing device |
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Granted publication date: 20151007 Effective date of abandoning: 20180413 |
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| AV01 | Patent right actively abandoned |