WO2016141886A1 - 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 - Google Patents
一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 Download PDFInfo
- Publication number
- WO2016141886A1 WO2016141886A1 PCT/CN2016/076097 CN2016076097W WO2016141886A1 WO 2016141886 A1 WO2016141886 A1 WO 2016141886A1 CN 2016076097 W CN2016076097 W CN 2016076097W WO 2016141886 A1 WO2016141886 A1 WO 2016141886A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- sugar cane
- membrane
- filtration
- cane juice
- juice
- Prior art date
Links
Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/02—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation containing fruit or vegetable juices
- A23L2/08—Concentrating or drying of juices
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
- A23L2/72—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by filtration
- A23L2/74—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter by filtration using membranes, e.g. osmosis, ultrafiltration
Definitions
- the invention relates to a production process of sugar cane juice drinking water and compound sugar cane juice beverage, and belongs to the technical field of deep processing of sugar cane juice.
- Sugar cane is an annual or perennial tropical and subtropical herb with high nutritional value. Sugar cane is rich in sugar and water, and the content of sucrose, glucose and fructose is as high as 12%. In addition, scientific analysis, sugar cane also contains a variety of amino acids, vitamins and proteins, fat, calcium, phosphorus, iron and other substances that are very beneficial to the body's metabolism. Ancient Chinese medical scientists also listed sugar cane as a “reinforcing drug”. Chinese medicine believes that sugar cane into the lungs, stomach two classics, has the special effect of clearing heat, Shengjin, Qiqi, Runzao, Bufeiyiwei, can treat the injury caused by fever, upset thirst, nausea and vomiting, lung dryness Cough and asthma. In addition, sugar cane can also be relieved by laxation, and drinking its juice can also alleviate alcoholism.
- Sugar cane juice refers to the juice produced after crushing sugar cane. Sugarcane juice is made into a beverage because of its high sugar content. It is not only easy to eat, but also has excellent taste. It can effectively preserve various nutrients beneficial to the human body in sugar cane. It is a good choice for sugarcane processing.
- Sugar cane drinking water refers to the clear liquid after sugar cane juice is removed, that is, the water contained in sugar cane. The sugar cane drinking water is used for compounding sugar cane juice beverage, which can maintain pure original flavor and is also very suitable. Drink directly. Sugar cane produced in China is mainly used to make sugar.
- the sugarcane juice processed by the conventional pressing process has a difficult problem to be solved, that is, the stability of fresh sugar cane juice is very poor, it is difficult to preserve for a long time, and it is easy to produce enzymatic browning, microbial contamination and colloidalization, which seriously affects The taste, therefore, fresh sugar cane juice is generally only suitable for freshly squeezed drinks, not suitable for the production of food and beverage.
- the patent document "Method for obtaining sugar cane-based juice and juice obtained and beverage containing the same discloses a method for obtaining fresh sugar cane juice with improved properties, which is applicable. For the preparation of food and beverage.
- the tangential filtration of the crude sugar cane juice is carried out at a cane juice temperature of 40-65 ° C using a filter membrane having a cut-off threshold in the range of 50 to 150 kg/mol or an average pore diameter ranging from 0.05 to 0.2 ⁇ m.
- a sugar cane juice suitable for preparing a beverage is added before pressing sugar cane. But the problem with this method is:
- the selected filter membrane is ultrafiltration membrane.
- the pore diameter is too small.
- the crude sugar cane juice just squeezed out is dirty and contains more bagasse. If you directly enter the ultrafiltration membrane with too small pore size, the membrane pores will be blocked quickly, resulting in low filtration efficiency, long time and high ultrafiltration membrane loss.
- sugar cane juice contains more plant protein, colloid, tannin, starch and other substances. If the cane juice is directly filtered at a temperature of 40-65 ° C, these substances cannot be effectively filtered out. These substances exist in sugar cane juice. On the other hand, it will affect the taste. On the other hand, if pasteurization is carried out later, the temperature will rise, and the protein, tannin and colloid will be precipitated. The sugar cane juice will become cloudy and the turbidity (NTU) will be The rapid rise to around 160 around 1.5 reduces the quality of sugar cane juice and is not conducive to long-term preservation.
- NTU turbidity
- the process contains a long step of the enzyme-killing step, on the one hand will affect the flavor of sugar cane juice, on the other hand, the longer process will increase production costs.
- the microfiltration membrane with larger pore size is selected for filtration, and the temperature of the cane juice is directly raised to a higher temperature of 80-100 ° C. Effectively removes plant protein, colloid, tannin, starch and other substances, and rapidly inactivates various enzymes that cause browning, and can also achieve filtration sterilization. At the same time, it can effectively preserve the beneficial substances such as polyphenols and octacosanol in sugar cane juice; on the other hand, the coarse filter can be used for pretreatment, and the microfiltration membrane used has a large pore size and high filtration temperature.
- the viscosity of the sugar cane juice is reduced, the filtration speed is greatly improved, and the time for the crude sugar cane juice to stay before entering the microfiltration step is short, and the sugar cane juice can be well controlled without adding heat treatment to the microwave or steam before pressing the sugar cane. Browning.
- the sugarcane juice is subjected to nanofiltration membrane separation and concentration, reverse osmosis membrane filtration and compounding, and the sugarcane juice supernatant filtered by the microfiltration membrane is concentrated into syrup, and the sugar cane juice drinking water is separated and filtered, and then sugar cane is taken.
- the juice drinking water is compounded with the concentrated syrup, which can control the sugar cane juice beverage with different sweetness ratio, minimize the original flavor of the sugar cane juice, and effectively remove the bitterness in the sugar cane juice.
- concentration with a nanofiltration membrane can effectively replace multi-effect evaporation concentration, reduce energy consumption, and also reduce production costs.
- the sugarcane drinking water obtained by filtering the nanofiltration liquid through the reverse osmosis membrane is pure natural plant water, which is beneficial to human health, that is, it can be directly used for drinking, and can also be used for compounding sugarcane juice beverage, thereby realizing effective for sugarcane water resources. use.
- the object of the present invention is to provide a novel production process of sugar cane drinking water and compound sugar cane juice beverage, which has the characteristics of short process flow, low energy consumption, small investment, small floor space, and the like, and products. Pure, non-polluting, high quality and healthier.
- a production process of sugar cane drinking water and compound sugar cane juice beverage characterized in that the following steps are included:
- A. Sugar cane juice The washed sugar cane is pressed by conventional pressing equipment to obtain coarse sugar cane juice;
- the crude sugar cane juice is pretreated by a filtering device to remove larger bagasse;
- Microfiltration membrane filtration The pretreated crude sugar cane juice is heated and sent to a microfiltration membrane for filtration.
- the microfiltration membrane adopts a ceramic membrane with a pore diameter of 300-1200 nm, and the temperature of the cane juice is 80-100 ° C during filtration.
- the pressure is 0.1-0.5 MPa, and the sugar cane juice supernatant having a sucrose concentration of 12-14 ° Bx is obtained;
- Nanofiltration membrane separation and concentration The sugarcane juice supernatant obtained by filtering through the microfiltration membrane is sent to a nanofiltration membrane for separation and concentration.
- the nanofiltration membrane adopts a nanofiltration membrane with a molecular weight cut off of 100-500 Da, and the filtration temperature is 50. ⁇ 80 ° C, filtration pressure is 1.0 ⁇ 4.0 MPa, thereby concentrating the sucrose concentration of the sugar cane juice supernatant to 30-32° Bx, forming a concentrated syrup of sugar cane juice, and separating the nanofiltration liquid, and the nanofiltration liquid is a sugar cane juice clearing liquid for removing more than 99% sugar;
- E. Reverse osmosis membrane filtration The nanofiltration membrane separated by the nanofiltration membrane is sent to the reverse osmosis membrane system for separation and filtration.
- the reverse osmosis membrane is made of high temperature resistant membrane, and the filtration temperature is 50-80 ° C, and the filtration pressure is 1.0. ⁇ 4.0 MPa, thereby further filtering the residual sugar of the nanofiltration solution and impurities such as monovalent ions to obtain a sugar cane drinking water that can be directly consumed;
- the sugar cane drinking water filtered by the reverse osmosis membrane and the concentrated sugar syrup obtained by concentrating the nanofiltration membrane are compounded according to different ratios to obtain different sweetness of raw sugar cane juice required by different people. Drink.
- the nanofiltration liquid separated by the nanofiltration membrane in the step D can also be directly
- the sugar cane juice concentrated syrup obtained by concentration through the nanofiltration membrane is compounded according to different ratios, and the raw sugar cane juice beverages with different sweetness required by different people are obtained.
- the sugar cane juice liquid obtained by filtering the microfiltration membrane in step C may be compounded with the nanofiltration liquid obtained in step D or the sugar cane drinking water obtained in step E according to different ratios to obtain different populations.
- Raw sweet cane juice beverages of different sweetness are required.
- the filtering device may be a security filter, a disc centrifuge or a high frequency vibrating screen.
- a disc centrifuge select a speed of 3000 ⁇ 12000r / min, preferably a speed of 10000r / min;
- a high frequency vibrating screen select the accuracy of 80 ⁇ 200 mesh, the frequency is 500 ⁇ 2000r / min, preferably The precision is 120 mesh and the frequency is 1200r/min, which can ensure the precision of preprocessing and obtain high processing capacity.
- the microfiltration membrane preferably has a pore diameter of 300 to 500 nm, the cane juice temperature is 90 to 95 ° C, the filtration pressure is 0.35 to 0.5 MPa, the optimal microfiltration membrane pore size is 500 nm, and the cane juice temperature is 95 ° C. The pressure is 0.4 MPa. Under this condition, the flux can be reduced slowly and the energy consumption is relatively low.
- the nanofiltration membrane is made of ceramic or polyether sulfone, polyamide high temperature resistant organic membrane, preferably the nanofiltration membrane has a pore size of 100 to 300 Da, the filtration temperature is 70 to 80 ° C, and the filtration pressure is 2.0 to 3.0. Mpa.
- the nanofiltration membrane has a pore size of 150 Da and the filtration temperature is 80 ° C, it can ensure high membrane flux and slow membrane fouling, and the membrane has high rejection of sucrose, sucrose.
- the extraction rate is above 99.9%.
- the filtration pressure is controlled at 3.0 MPa, the membrane flux is large, which can ensure the production efficiency and the membrane flux is easy to recover.
- the reverse osmosis membrane is made of polyethersulfone or polyamide, and the filtration temperature is preferably 70 to 80 ° C, and the filtration pressure is 2.0 to 3.0 MPa.
- the filtration pressure is controlled at 3.0 MPa, the membrane flux is large, the membrane contamination is slow, and the maximum production efficiency can be ensured.
- additives such as honey, puerarin extract, honeysuckle extract, Dendrobium candidum extract, vitamin C, vitamin E and the like may be added to obtain more different kinds of sugar cane juice beverages.
- the process of the invention uses the microfiltration membrane and the nanofiltration membrane to clarify and concentrate the sugar cane juice, and can retain the naturalness of the sugarcane juice to a greater extent.
- the taste is high, the degree of automation is high, the labor cost can be saved by 80%, the energy consumption is reduced, the energy saving and the emission reduction are achieved, and the economic benefit is remarkable.
- the process flow of the invention is shorter and the control process is simpler.
- the sugarcane juice is clarified, it is also provided with nanofiltration membrane separation and concentration, reverse osmosis membrane filtration and compounding, which can obtain concentrated syrup for transportation, and can remove about 50% of monovalent ions, which can remove sugarcane well.
- the bitterness in the juice while making full use of the sugar cane itself, can be obtained directly drinking pure natural sugar cane drinking water, can also be compounded into any different sweetness of the original sugar cane juice drink to meet the needs of different groups of people.
- the invention adopts the microfiltration membrane to filter, the microorganisms such as bacteria can be directly filtered out, and the obtained clarified product does not need to be pasteurized again in the subsequent process, thereby maintaining the original flavor of the sugarcane juice and reducing the original flavor. Production steps to reduce production costs.
- the sugar cane drinking water produced by the process of the invention is pure natural plant water, beneficial to the human body, meets the national bottled drinking water standard, and realizes the resource utilization of the sugar cane.
- the sugar cane juice beverage compounded by the method of the invention can effectively preserve various natural beneficial substances such as natural pigment, polyphenol and octacosanol in sugar cane juice, does not contain bitter taste, has good taste and is rich in nutrients. , resistant to preservation, the finished product is put After half a year, there was no deterioration.
- 1 is a flow chart showing the production process of the sugar cane drinking water and the compounded sugar cane juice beverage of the present invention.
- a method for producing a sugar cane juice beverage according to a conventional process is first introduced, specifically: first, the sugar cane is pressed through a pressing device to obtain a crude sugar cane juice; and the coarse sugar cane juice is passed through a trommel sieve and a 20-mesh filter sieve to remove the bagasse.
- the traditional method for producing sugar cane juice beverage has complicated process and high energy consumption. It also contains sulfur dioxide harmful to human body. The most important thing is that it is not resistant to preservation. Sometimes it has bitter taste, poor taste and lack of original sugar cane. Therefore, Lost the unique flavor of natural sugar cane juice.
- the specific implementation of the sugar cane drinking water and the compounded sugar cane juice beverage produced according to the process of the present invention is as follows.
- the sugarcane drinking water and the compounded sugarcane juice beverage are produced according to the following process:
- A. Sugar cane juice The washed sugar cane is pressed by conventional pressing equipment to obtain coarse sugar cane juice;
- Pretreatment of crude sugar cane juice The crude sugar cane juice is pretreated by a disc centrifuge to remove larger bagasse, and the speed of the disc centrifuge is 10000 r/min;
- Microfiltration membrane filtration the pretreated crude sugar cane juice is heated and sent to a microfiltration membrane for filtration.
- the microfiltration membrane adopts a ceramic membrane with a pore diameter of 300 nm, the temperature of the cane juice is 90 ° C, and the filtration pressure is 0.5 MPa.
- the sucrose clear juice obtained by filtration through the microfiltration membrane is sent to a nanofiltration membrane for separation and concentration, and the nanofiltration membrane Using a high temperature resistant polyamide nanofiltration membrane with a molecular weight cut off of 500 Da, the filtration pressure is 1.0 MPa, and the sucrose concentration of the sugar cane juice supernatant is concentrated to 30 ° Bx to form a sugar cane juice concentrated syrup;
- Reverse osmosis membrane filtration The nanofiltration membrane separated by the nanofiltration membrane is sent to the reverse osmosis membrane system for separation and filtration.
- the reverse osmosis membrane is made of high temperature resistant polyamide membrane, the filtration temperature is 50 ° C, and the filtration pressure is 1.0 MPa. To obtain drinking water for sugar cane that can be directly consumed;
- the sugar cane drinking water produced through the above steps is pure natural plant water, which is clear and transparent and meets the national standard for bottled drinking water.
- the sugarcane juice beverage produced by the above steps has not been detected as sulfur dioxide content, and has been biochemically tested to be sterile, meeting national food safety standards, and the beverage has less sugar content, has a special aroma of sugar cane, and has a pure taste.
- the sugarcane drinking water and the compounded sugarcane juice beverage are produced according to the following process:
- A. Sugar cane juice The washed sugar cane is pressed by conventional pressing equipment to obtain coarse sugar cane juice;
- the crude sugar cane juice is pretreated by a high frequency vibrating screen with a precision of 120 mesh and a frequency of 1200 r/min to remove large bagasse;
- Microfiltration membrane filtration The pretreated crude sugar cane juice is heated and sent to a microfiltration membrane for filtration.
- the microfiltration membrane adopts a ceramic membrane with a pore diameter of 1200 nm, the temperature of the cane juice is 100 ° C, and the filtration pressure is 0.1 MPa.
- Nanofiltration membrane separation and concentration The sucrose clear juice obtained by filtering through the microfiltration membrane is sent to a nanofiltration membrane for separation and concentration, and the nanofiltration membrane adopts a ceramic nanofiltration membrane with a molecular weight cutoff of 100 Da, and the filtration pressure is 4.0 MPa, and The sucrose concentration of the sugar cane juice supernatant is concentrated to 28 ° Bx to form a sugar cane juice concentrated syrup;
- Reverse osmosis membrane filtration The nanofiltration membrane separated by the nanofiltration membrane is sent to the reverse osmosis membrane system for separation and filtration.
- the reverse osmosis membrane is made of high temperature resistant polyamide membrane, the filtration temperature is 80 ° C, and the filtration pressure is 3.0 MPa. To obtain drinking water for sugar cane that can be directly consumed;
- the sugar cane drinking water produced through the above steps is pure natural plant water, which is clear and transparent and meets the national standard for bottled drinking water.
- the sugarcane juice beverage produced by the above steps has not been detected in sulfur dioxide content. It has been biochemically tested to be sterile, meets national food safety standards, and has a sweet and mellow taste. It has a special aroma of sugar cane and is pure in taste. It is suitable for sweet drinks. People drink.
- the sugarcane drinking water and the compounded sugarcane juice beverage are produced according to the following process:
- A. Sugar cane juice The washed sugar cane is pressed by conventional pressing equipment to obtain coarse sugar cane juice;
- Pretreatment of crude sugar cane juice The crude sugar cane juice is pretreated through a 200-mesh security filter to remove larger bagasse;
- Microfiltration membrane filtration The pretreated crude sugar cane juice is heated and sent to a microfiltration membrane for filtration.
- the microfiltration membrane adopts a ceramic membrane with a pore diameter of 500 nm, the temperature of the cane juice is 95 ° C, and the filtration pressure is 0.4 MPa.
- a sugar cane juice serum having a sucrose concentration of 13.5%;
- Nanofiltration membrane separation and concentration The sucrose clear juice obtained by filtering through the microfiltration membrane is sent to a nanofiltration membrane for separation and concentration, and the nanofiltration membrane adopts a polyamide nanofiltration membrane with a molecular weight cutoff of 150 Da, and the filtration pressure is 3.0 MPa, and Concentrating the sucrose concentration of the sugar cane juice supernatant to 32° Bx to form a sugar cane juice concentrated syrup;
- Reverse osmosis membrane filtration The nanofiltration membrane separated by the nanofiltration membrane is sent to the reverse osmosis membrane system for separation and filtration.
- the reverse osmosis membrane is made of high temperature resistant polyamide membrane, the filtration temperature is 70 ° C, and the filtration pressure is 2.0 MPa. To obtain drinking water for sugar cane that can be directly consumed;
- the sugar cane drinking water filtered by the reverse osmosis membrane and the concentrated sugar syrup obtained by concentrating the nanofiltration membrane are mixed into a 1# sugar cane juice beverage having a sugar content of 3° Bx; the nanofiltration membrane is separated.
- the obtained nanofiltration liquid is directly mixed with the sugar cane juice concentrated syrup obtained by concentrating the nanofiltration membrane to prepare a 2# sugar cane juice beverage having a sugar content of 3° Bx.
- the sugar cane drinking water produced through the above steps is pure natural plant water, which is clear and transparent and meets the national standard for bottled drinking water.
- the 1# sugarcane juice beverage produced by the above steps has not been detected as sulfur dioxide content, and has been biochemically tested as sterile to meet national food safety standards; the 2# sugarcane juice beverage produced by the above steps has not been detected. After biochemistry The test is sterile and meets national food safety standards.
- the two blended sugar cane juice drinks are light in sweetness, have a special aroma of sugar cane, and have a pure taste. They are suitable for people who like light and sweet drinks.
Landscapes
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Water Supply & Treatment (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Non-Alcoholic Beverages (AREA)
Abstract
Description
Claims (8)
- 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺,其特征在于包括以下步骤:A、甘蔗榨汁:应用常规压榨设备将清洗后的甘蔗进行压榨,得到粗甘蔗汁;B、粗甘蔗汁预处理:将粗甘蔗汁通过过滤装置进行预处理,去除较大的蔗渣;C、微滤膜过滤:将经预处理过的粗甘蔗汁加热后送入微滤膜进行过滤,微滤膜采用孔径为300~1200nm的陶瓷膜,过滤时蔗汁温度为80~100℃,过滤压力为0.1~0.5MPa,得到蔗糖浓度为12~14°Bx的甘蔗汁清液;D、纳滤膜分离浓缩:将经微滤膜过滤后得到的甘蔗汁清液送入纳滤膜进行分离浓缩,纳滤膜采用截留分子量为100~500Da的纳滤膜,其过滤温度为50~80℃,过滤压力为1.0~4.0MPa,从而将甘蔗汁清液的蔗糖浓度浓缩到30~32°Bx,形成甘蔗汁浓缩糖浆,并分离出纳滤清液,纳滤清液为脱除99%以上糖分的甘蔗汁清液;E、反渗透膜过滤:将经纳滤膜分离出的纳滤清液,送入反渗透膜系统进行分离过滤,反渗透膜采用耐高温膜,其过滤温度50~80℃,过滤压力为1.0~4.0MPa,从而将纳滤清液的剩余糖分和一价离子杂质进一步滤除,得到可直接饮用的甘蔗饮用水;F、复配:将经反渗透膜过滤得到的甘蔗饮用水和经纳滤膜浓缩后得到的甘蔗汁浓缩糖浆按不同配比进行复配,得到不同人群需要的不同甜度的原汁甘蔗汁饮料。
- 根据权利要求1所述的生产工艺,其特征是:所述步骤D中经纳滤膜分离出的纳滤清液和经纳滤膜浓缩后得到的甘蔗汁浓缩糖浆按不同配比进行复配,得到不同人群需要的不同甜度的原汁甘蔗汁饮料。
- 根据权利要求1所述的生产工艺,其特征是:所述步骤C经微滤膜过滤后得到的甘蔗汁清液与步骤D得到的纳滤清液或步骤E得到的甘蔗饮用水按不同配比进行复配,得到不同人群需要的不同甜度的原汁甘蔗汁饮料。
- 根据权利要求1所述的生产工艺,其特征是:所述步骤B中,过滤装置采用保安过滤器或碟式离心机或高频振动筛,当采用碟式离心机时,其转速为3000~12000r/min,当采用高频 振动筛时,其精度为80~200目,频率为500~2000r/min。
- 根据权利要求1所述的生产工艺,其特征是:所述步骤C中,微滤膜孔径为300~500nm,蔗汁温度为90~95℃,过滤压力为0.35~0.5MPa。
- 根据权利要求1所述的生产工艺,其特征是:所述步骤D中,纳滤膜采用陶瓷类或聚醚砜、聚酰胺类耐高温有机膜,纳滤膜孔径为100~300Da,过滤温度为70~80℃,过滤压力为2.0~3.0Mpa。
- 根据权利要求1所述的生产工艺,其特征是:所述步骤E中,反渗透膜采用聚醚砜类或聚酰胺类材质,过滤温度为70~80℃,过滤压力为2.0~3.0Mpa。
- 根据权利要求1或2或3所述的生产工艺,其特征是:复配甘蔗汁饮料时,还加入蜂蜜、葛根提取物、金银花提取物、铁皮石斛提取物、维生素C、维生素E作为添加剂进行复配。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2016228592A AU2016228592B2 (en) | 2015-03-11 | 2016-03-10 | Process for producing sugar cane potable water and blended sugar cane juice beverage |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510105754.8A CN104643221B (zh) | 2015-03-11 | 2015-03-11 | 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 |
CN201510105754.8 | 2015-03-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2016141886A1 true WO2016141886A1 (zh) | 2016-09-15 |
Family
ID=53235270
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2016/076097 WO2016141886A1 (zh) | 2015-03-11 | 2016-03-10 | 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 |
Country Status (3)
Country | Link |
---|---|
CN (1) | CN104643221B (zh) |
AU (1) | AU2016228592B2 (zh) |
WO (1) | WO2016141886A1 (zh) |
Families Citing this family (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104643221B (zh) * | 2015-03-11 | 2017-07-07 | 广西叶茂机电自动化有限责任公司 | 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 |
CN105076564A (zh) * | 2015-07-23 | 2015-11-25 | 李博 | 一种功能性保健饮料及其制备方法 |
CN105603130B (zh) * | 2015-10-28 | 2019-07-19 | 中国科学院过程工程研究所 | 一种甘蔗制糖过程中残糖的回收装置及方法 |
CN105734177B (zh) * | 2016-03-11 | 2020-08-11 | 广西叶茂食品有限责任公司 | 一种全营养纯净粉糖和液体糖浆的工业化生产工艺及设备 |
CN107435084A (zh) * | 2016-05-25 | 2017-12-05 | 中国科学院过程工程研究所 | 一种利用多级膜过滤对甘蔗糖蜜进行精制的工艺 |
CN106174584A (zh) * | 2016-06-29 | 2016-12-07 | 韦智涛 | 一种铁皮石斛糖浆的制备方法 |
CN106071497A (zh) * | 2016-06-29 | 2016-11-09 | 韦智涛 | 一种铁皮石斛饮料的制备方法 |
CN106509521A (zh) * | 2016-09-24 | 2017-03-22 | 合肥信达膜科技有限公司 | 一种果汁分离浓缩膜处理技术 |
CN107460081A (zh) * | 2017-09-21 | 2017-12-12 | 广西叶茂食品有限责任公司 | 一种利用纳滤甘蔗汁制备甘蔗果酒的方法 |
CN107744078A (zh) * | 2017-11-21 | 2018-03-02 | 厦门市天泉鑫膜科技股份有限公司 | 一种西兰花功能饮料及制备方法和设备 |
CN110651922A (zh) * | 2019-10-24 | 2020-01-07 | 齐迹科技有限责任公司 | 一种富含二十八烷醇甘蔗水的生产方法 |
CN110651920A (zh) * | 2019-10-24 | 2020-01-07 | 齐迹科技有限责任公司 | 一种富含二十八烷醇甘蔗水的生产工艺 |
CN110651921A (zh) * | 2019-10-24 | 2020-01-07 | 齐迹科技有限责任公司 | 一种甘蔗水生产工艺 |
CN111657410A (zh) * | 2020-06-29 | 2020-09-15 | 广西科技师范学院 | 一种桑葚-甘蔗复合饮料及其制作方法 |
CN113575802A (zh) * | 2021-07-28 | 2021-11-02 | 良品铺子营养食品有限责任公司 | 一种减糖果汁及其制备方法 |
CN114052152B (zh) * | 2021-09-28 | 2023-05-09 | 海南黎草纪新生物科技有限公司 | 一种植物小分子水的提取方法 |
CN114891930A (zh) * | 2022-02-21 | 2022-08-12 | 江苏久吾高科技股份有限公司 | 一种甘蔗植株细胞饮用水联产高品质原生态红糖的方法 |
CN114891931A (zh) * | 2022-03-01 | 2022-08-12 | 江苏久吾高科技股份有限公司 | 一种甘蔗植株细胞饮用水联产高品质姜味红糖的工艺 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1144062A (zh) * | 1995-08-25 | 1997-03-05 | 付佑林 | 一种天然甘蔗汁的生产方法 |
CN102489155A (zh) * | 2011-11-15 | 2012-06-13 | 广西大学 | 多级膜并行生产营养糖、风味蔗汁及饲料原料的方法 |
CN103710469A (zh) * | 2013-12-26 | 2014-04-09 | 江苏久吾高科技股份有限公司 | 一种可直接食用糖浆的生产工艺及装置 |
CN103725802A (zh) * | 2013-12-27 | 2014-04-16 | 江苏久吾高科技股份有限公司 | 一种蔗糖精制的工艺 |
CN104643221A (zh) * | 2015-03-11 | 2015-05-27 | 广西叶茂机电自动化有限责任公司 | 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009044965A (ja) * | 2007-08-14 | 2009-03-05 | Okinawa Pref Gov | サトウキビ機能性エキスおよびその製造方法 |
-
2015
- 2015-03-11 CN CN201510105754.8A patent/CN104643221B/zh active Active
-
2016
- 2016-03-10 WO PCT/CN2016/076097 patent/WO2016141886A1/zh active Application Filing
- 2016-03-10 AU AU2016228592A patent/AU2016228592B2/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1144062A (zh) * | 1995-08-25 | 1997-03-05 | 付佑林 | 一种天然甘蔗汁的生产方法 |
CN102489155A (zh) * | 2011-11-15 | 2012-06-13 | 广西大学 | 多级膜并行生产营养糖、风味蔗汁及饲料原料的方法 |
CN103710469A (zh) * | 2013-12-26 | 2014-04-09 | 江苏久吾高科技股份有限公司 | 一种可直接食用糖浆的生产工艺及装置 |
CN103725802A (zh) * | 2013-12-27 | 2014-04-16 | 江苏久吾高科技股份有限公司 | 一种蔗糖精制的工艺 |
CN104643221A (zh) * | 2015-03-11 | 2015-05-27 | 广西叶茂机电自动化有限责任公司 | 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 |
Also Published As
Publication number | Publication date |
---|---|
CN104643221A (zh) | 2015-05-27 |
AU2016228592A1 (en) | 2017-11-02 |
CN104643221B (zh) | 2017-07-07 |
AU2016228592B2 (en) | 2019-04-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2016141886A1 (zh) | 一种甘蔗饮用水及复配甘蔗汁饮料的生产工艺 | |
Lipnizki | Cross‐flow membrane applications in the food industry | |
US9730465B2 (en) | Plant based beverages, and methods for preparation thereof | |
CN104489827A (zh) | 一种甘蔗浓缩汁的加工工艺 | |
CN104738755B (zh) | 一种多级膜并行生产甘蔗浓缩汁及甘蔗饮用水的方法 | |
CA2798559C (en) | Plant-based electrolyte compositions | |
CN104824760B (zh) | 一种甘蔗活性饮用水及纯甘蔗原汁饮料的生产工艺 | |
CN107619740A (zh) | 一种纯蜂蜜发酵中度酒的制备方法 | |
CN104720071A (zh) | 一种甘蔗汁固体饮料的加工装置 | |
Karmakar et al. | Pectin removal and clarification of juices | |
CN205409475U (zh) | 一种多级混合膜滤固体蔗汁加工装置 | |
Cassano et al. | Integration of membrane technologies into conventional existing systems in the food industry | |
CN105124689A (zh) | 一种胭脂红萝卜浓缩汁产品的加工方法及应用 | |
Cassano et al. | Reverse osmosis in food processing | |
CN104839827B (zh) | 一种多级膜并行生产甘蔗浓缩汁及甘蔗饮用水的装置 | |
Vatai | Separation technologies in the processing of fruit juices | |
CN204579790U (zh) | 一种多级膜并行生产甘蔗浓缩汁及甘蔗饮用水的装置 | |
CN204682444U (zh) | 一种甘蔗汁固体饮料的加工装置 | |
CN106119430A (zh) | 一种富多酚黑糖的生产线 | |
CN104997092A (zh) | 一种白萝卜浓缩汁的加工工艺 | |
CN204351015U (zh) | 一种甘蔗浓缩汁的加工装置 | |
Malik et al. | Membrane separation technology in food and allied industry. | |
Kulcan et al. | Changes in turbidity, total phenolic and anthocyanin contents of clear red grape juice during processing. | |
CN107362278A (zh) | 一种祛风止痛的中医组方保健药酒及其制备方法 | |
CN104250610A (zh) | 一种西枸杞脱醇保健酒 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 16761113 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
ENP | Entry into the national phase |
Ref document number: 2016228592 Country of ref document: AU Date of ref document: 20160310 Kind code of ref document: A |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 16761113 Country of ref document: EP Kind code of ref document: A1 |