WO2013026313A1 - 甘蔗制糖新助剂、制备方法及在制糖生产中的应用方法 - Google Patents
甘蔗制糖新助剂、制备方法及在制糖生产中的应用方法 Download PDFInfo
- Publication number
- WO2013026313A1 WO2013026313A1 PCT/CN2012/077024 CN2012077024W WO2013026313A1 WO 2013026313 A1 WO2013026313 A1 WO 2013026313A1 CN 2012077024 W CN2012077024 W CN 2012077024W WO 2013026313 A1 WO2013026313 A1 WO 2013026313A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- sugar
- new
- weight
- parts
- sugarcane
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/12—Purification of sugar juices using adsorption agents, e.g. active carbon
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/08—Purification of sugar juices by oxidation or reduction
Definitions
- the invention relates to an auxiliary agent, in particular to a new sugarcane sugar auxiliaries, a preparation method and a application method in sugar production.
- the cleaning process is the focus of the sugar production process. Because the amount of sugar cane juice that the sugar factory needs to process every day is very large, it is thousands of tons, more than 10,000 tons, and the sugar cane juice is one.
- the multi-component solution itself is a colloid. At the same time, due to various conditions, the components contained are apt to change, unstable, and often undergo complex physico-chemical changes, bringing many unexpected effects to the purification process. Difficulties.
- the world's sugar industry generally uses a large amount of sulfur dioxide produced by burning sulfur as the main refining agent to sulphurize the sugar cane juice for decolorization and clarification, or use carbon dioxide as a refining agent and sulfur dioxide as a supplement to carry out decolorization and clarification treatment. Therefore, the sugar factory produces white sugar with more or less residual sulfur. Sulfur dioxide and its derivatives are carcinogens. The white sugar produced now contains residual sulfur dioxide derivatives in addition to the harmful substances containing residual sulfur. However, the current white sugar test does not require the detection of sulfur dioxide derivatives, so the sugar products There are still food safety hazards.
- the technical problem to be solved by the present invention is that, in view of the prior art, the use of sulfur dioxide to decolorize and clarify sugarcane juice causes defects in sulfur dioxide and its derivatives in white sugar, and provides a new type of sugar cane juice without using sulfur. It is a new additive for sugar cane sugar that is decolorized and clarified, safe and has no harmful residue.
- a further technical problem to be solved by the present invention is to provide a scientific, safe, effective and multi-selective method for preparing a new sugar-making auxiliary.
- the technical problem to be solved by the present invention is to provide a process for completely eliminating the sulfur-smoke neutralization section on the basis of the existing sugar-making process, and to efficiently treat the sugar liquid without using sulfur, thereby obtaining a higher quality clear juice with less investment.
- a new sugarcane sugar auxiliaries including the following raw materials by weight: concentrated phosphoric acid 100, chitosan 0.5-50.
- sugar cane sugar new adjuvant further comprises 0.5-8 parts by weight of zinc lactate, zinc citrate or zinc sulfate.
- sugarcane sugar new adjuvant further comprises acetic acid in an amount of 1-9.6 parts by weight.
- sugar cane sugar new adjuvant further comprises 15-90 parts by weight of diatomaceous earth.
- the first method for preparing a new sugarcane sugar auxiliary weigh 100 parts by weight of concentrated phosphoric acid, 0.5-50 parts by weight of chitosan, and react at 8-300 ° C for 30-120 minutes to obtain sugar cane sugar new aid.
- the agent is a high-fiber polyphosphate polymer compound with a strong positive charge.
- a second method for preparing a sugar cane sugar new additive comprising the following steps:
- the high-fiber polyphosphate polymer compound is added with 0.5-8 parts by weight of zinc lactate, zinc citrate or zinc sulfate, and stirred to obtain a liquid sugar cane sugar new additive.
- the third method for preparing a new sugarcane sugar auxiliary comprises the following steps:
- the first application method of sugar cane sugar new additive in sugar production includes:
- the cane crushing section the cane is subjected to multiple presses to obtain multiple presses, at least one of the press juices is added to the above sugar cane sugar new additive for stirring, or in multiple presses Adding the above-mentioned sugar cane sugar new additive to the mixed juice formed after the juice is mixed, and the sugar cane sugar is mixed.
- the new additive is added in an amount of 0.2-1.5 kg/m 3 and controls the pH of the pressed juice or the mixed juice to be 6.8-8.5;
- the pre-ash juice of the section is heated to 50-85 ° C, and the new sugarcane sugar auxiliaries are put into the amount of 0.025-1 kg/m; Control between 7-7.5; then heat the pre-gray to 95-105 ° C, add flocculant 0.5 ⁇ 5ppm, slow stirring, so that very small suspensions are fully exposed to positively charged sugar cane sugar additives, followed by Enter the sedimentation tank and clear it to obtain clear juice.
- the application of the new sugarcane sugar auxiliaries in sugar production further includes the application after the purification process: adding the fresh sugarcane sugar-making auxiliaries to the clear juice processed in the clean process at a rate of 0.02-0.1 kg/m. Re-treatment, adjust the pH value with calcium sulphate, control and control the pH value at 6.9-7.3, and filter to obtain higher quality clear juice;
- the application of the new sugarcane sugar auxiliaries in sugar production further includes application in the production process of the syrup: adding the sugar cane sugar to the sugar syrup in the amount of 0.05-0.6 kg/m 3
- the auxiliaries are reprocessed, the pH is adjusted with calcium saccharate, the pH is controlled at 6.2-7.0, and the high-purity syrup is obtained by filtration.
- the second application method of sugar cane sugar new additive in sugar production is applied to sugar cane crushing section: sugar cane is pressed by multiple presses to obtain multiple press juices, and at least one of the pressed juices is added to the above sugar cane.
- the third application method of sugar cane sugar new additive in sugar production is applied to the refining section: The pre-ash juice of the section is heated to 50-85 ° C, and the sugar cane is put into the above according to the amount of 0.025-1 kg/m.
- Sugar new help The agent is operated to the neutralization process to control the pH value between 7 and 7.5; then the pre-ash juice is heated to 95-105 ° C, the flocculant is added 0.5 to 5 ppm, and the stirring is slow, so that the extremely small suspension is fully contacted.
- a new additive for sugar cane sugar which then enters the settling tank and is cleaned to give clear juice.
- the main raw materials for the new sugar-making auxiliaries of the present invention are concentrated phosphoric acid and chitosan, and the two are reacted in an environment of 8-300 ° C, the phosphoric acid is gradually dehydrated to synthesize polyphosphoric acid, and a certain amount of polyphosphoric acid can be formed.
- an appropriate amount of zinc lactate, zinc citrate or zinc sulfate and an appropriate amount of acetic acid are added.
- the intensity of hydrogen phosphate ion increases with condensation, and the strength of the amino group bonded to the hydrogen ion of the polymer chain to form a positive charge of NH 3 + is enhanced, and other active groups and chains are activated.
- the chemical activity of the active center Finally, an appropriate amount of diatomaceous earth is added to adsorb the reaction product to make it highly intensive, thereby further enhancing the function of each product.
- the new additive produced has excellent physical and chemical properties. detailed description
- the first new sugarcane sugar auxiliaries including the following parts by weight: concentrated phosphoric acid 100, chitosan 0.5-50.
- the sugarcane sugar new additive is a basic auxiliary agent, and the above raw material is prepared to obtain a reaction product-high-fiber polyphosphate polymer compound with strong positive charge, which can function as a clarification and decolorization treatment of the sugar cane juice.
- Table 1 Concentrated Phosphoric Acid Chitosan Reaction Time Reaction Temperature Example 1 100 0.5 120min 8°C
- Example 2 100 30 30min 300 °C
- the first method for preparing a new sugar cane sugar granule is as follows: weigh 100 parts by weight of concentrated phosphoric acid, 0.5-50 parts by weight of chitosan, and react at 8-300 ° C for 30-120 minutes to obtain new sugar cane sugar.
- the additive is a high-fiber polyphosphate polymer compound with a strong positive charge.
- Table 1 The specific reaction conditions for each example are shown in Table 1.
- the second sugar cane sugar new additive including the following parts by weight of raw materials: concentrated phosphoric acid 100, chitosan 0.5-50, zinc lactate 0.5-8, zinc lactate can also be replaced by zinc citrate or zinc sulfate.
- the second sugar cane sugar new additive is based on the first new sugarcane sugar auxiliaries, which increases zinc lactate and improves the adsorption and clarification ability of the new sugarcane sugar auxiliaries.
- a second method for preparing a sugar cane sugar new additive comprising the following steps:
- the third new sugarcane sugar auxiliaries are based on the addition of a new sugarcane sugar auxiliaries to vinegar as a preservative.
- the amount of acetic acid added is 1-9.6 parts by weight.
- Zinc lactate can be replaced by zinc citrate.
- the third method for preparing a new sugarcane sugar auxiliary comprises the following steps:
- the fourth new sugarcane sugar auxiliaries are based on the third new sugarcane sugar auxiliaries, adding 15-90 parts by weight of diatomaceous earth, and the diatomaceous earth is preferably larger than the surface and porous.
- the fineness (particle size) of the diatomaceous earth is 40-120 mesh. The fineness of the diatomaceous earth can be selected as long as it is within the above range.
- Table 4 Concentrated phosphoric acid ⁇ 3 ⁇ 4 1 ⁇ according to the reaction time of the zinc lactate acetonitrile reaction time
- Example 12 100 1 3 2 15 120 min 8 ° C
- Example 13 100 8 0.5 1 20 95 min 60 ° C
- Example 14 100 12 8 9.6 57 LOOmin 80 °C
- Example 15 100 35 5 5 90 115 min 10 ° C
- Example 16 100 20 2 4 80 30 min 300 ° C
- Example 17 100 45 7 9 65 55 min 220 °C
- the fourth cane sugar new additive The preparation method comprises the following steps:
- the fifth sugar cane sugar new additive is based on the first sugar cane sugar new additive, adding diatomaceous earth 15-90 parts by weight of diatomaceous earth.
- the diatomaceous earth has a fineness of 40 to 120 mesh.
- Table 5 The specific raw materials and reaction conditions are shown in Table 5.
- Example 19 100 44 45 38min 290 °C
- the sixth new sugarcane sugar auxiliaries are based on the second sugar cane sugar new additive, adding diatomaceous earth 15-90 parts by weight of diatomaceous earth.
- the diatomaceous earth has a fineness of 40 to 120 mesh.
- the specific raw materials and reaction conditions are shown in Table 6.
- At least one of zinc citrate (zinc citrate or zinc sulphate), acetic acid and diatomaceous earth may be at least one of the first sugar cane sugar auxiliaries, and may be the sugar cane sugar of the present invention.
- the new auxiliaries are not listed here.
- the cane crushing section the cane is subjected to multiple presses to obtain multiple presses, at least one of the press juices is added to the above sugar cane sugar new additive for stirring, or in multiple presses Adding the sugarcane sugar auxiliaries of Examples 1 to 23 to the mixed juice formed after the juice mixing, the sugarcane sugar auxiliaries are added in an amount of 0.2-1.5 kg/m 3 , and the pressed juice is controlled or The pH of the mixed juice is 6.8-8.5;
- the pre-gray juice of the section is heated to 50-85 ° C, and the new sugarcane sugar auxiliaries of Examples 1 to 23 are put into the amount of 0.025-1 kg/m 3 ; Neutralization process Manufactured between 7 and 7.5; then the pre-gray is heated to 95-105 ° C, added flocculant 0.5 ⁇ 5ppm, slow stirring, so that very small suspensions are fully exposed to the positive charge of sugar cane sugar additives, followed by Enter the sedimentation tank and clear it to obtain clear juice.
- the addition of the new sugarcane sugar auxiliaries of Examples 1 to 23 in the above-mentioned section of the sugar production process can be used to achieve higher levels of finished sugar. See Table 7 for the specific amount of sugarcane sugar additives and reaction conditions.
- the application of the new sugarcane sugar auxiliaries after the cleaning process is also included: On the basis of Examples 24 to 27, the clear juice treated in the clean process is 0.02-0.1 kg/m. The amount of 3 was added to the sugarcane new auxiliaries of Examples 1 to 23 for further treatment, and the pH was adjusted with calcium saccharate to control the pH at 6.9-7.3, and filtered to obtain a higher quality clear juice. The addition amount of the new sugarcane sugar additive was 0.05 kg/m 3 , 0.02 kg/m 0.1 kg/m 3 and 0.08 kg/m 3 , respectively .
- the new sugarcane sugar auxiliaries are used, and the new sugarcane sugar auxiliaries are further applied in the syrup production process: 0.05 ⁇ 0.6 in the clear syrup
- the amount of kg/m was added to the new sugarcane auxiliaries of Examples 1 to 23 for further treatment, and the pH was adjusted with calcium saccharate to control the pH at 6.2-7.0, and filtered to obtain a high-purity syrup.
- the addition amount of the new sugarcane sugar additive was 0.05 kg/m 3 , 0.09 kg/m 3 , 0.12 kg/m 3 , and 0.2 kg/m 3 , respectively .
- sugarcane new auxiliaries of the present invention simultaneously or in sections or in combination in four sections, the purity of the sugar liquid is significantly improved, thereby producing more and better white granulated sugar.
- the second application method of sugar cane sugar new additive in sugar production is applied to sugar cane crushing section: sugar cane is pressed by multiple presses to obtain multiple press juices, and at least one of the pressed juices is added to the above sugar cane.
- the use amount and reaction conditions of the specific sugarcane sugar auxiliaries are shown in Table 8.
- the third application method of sugar cane sugar new additive in sugar production is applied to the refining section:
- the pre-ash juice of the section is heated to 50-85 ° C, and the sugar cane is put into the above according to the amount of 0.025-1 kg/m.
- New sugar additives run to neutralization process to control the pH between 7-7.5; then heat the pre-ash to 95-105 ° C, add flocculant 0.5 ⁇ 5ppm, slow stirring, make very small suspension
- Fully contact with positively charged sugar cane A new additive for sugar, which then enters the settling tank and is cleaned to give clear juice. See Table 9 for the specific amount of sugarcane sugar additives and reaction conditions.
- Table 11 is the data obtained by detecting various embodiments of the present invention, and it is known from the table:
- the plant After the mill season lasts for 100 days and the sugar price is not less than 7,000 yuan, the plant can increase the profit of 14 million yuan in one year. It can be seen from the following Table 11 that the simple purity of the embodiment of the present invention is 2.84 AP higher than the simple purity of the new sugar-free auxiliaries of the present invention. It can be seen that the application of the new sugarcane sugar auxiliaries will bring very much to the sugar factory. Considerable economic benefits.
- the sugar-free auxiliary agent of the invention is not added, and the new sugarcane sugar-making additive of the invention is added.
- PH hammer is also everywhere ⁇ ⁇ ⁇ Calcium at the simple value of the pure degree of purity pure original value salt purity degree before and after sugar degree ° °
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Jellies, Jams, And Syrups (AREA)
- Non-Alcoholic Beverages (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NZ621417A NZ621417B2 (en) | 2011-08-24 | 2012-06-15 | New additive for sugar manufacturing with cane, and preparation method therefor and application method thereof in sugar manufacturing |
AU2012300037A AU2012300037B2 (en) | 2011-08-24 | 2012-06-15 | New additive for sugar manufacturing with cane, and preparation method therefor and application method thereof in sugar manufacturing |
ZA2014/01646A ZA201401646B (en) | 2011-08-24 | 2014-03-05 | New additive for sugar manufacturing with cane, and preparation method therefor and application method thereof in sugar manufacturing |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110248232.5A CN102952904B (zh) | 2011-08-24 | 2011-08-24 | 甘蔗制糖新助剂、制备方法及在制糖生产中的应用方法 |
CN201110248232.5 | 2011-08-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2013026313A1 true WO2013026313A1 (zh) | 2013-02-28 |
Family
ID=47745902
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/CN2012/077024 WO2013026313A1 (zh) | 2011-08-24 | 2012-06-15 | 甘蔗制糖新助剂、制备方法及在制糖生产中的应用方法 |
Country Status (5)
Country | Link |
---|---|
CN (1) | CN102952904B (zh) |
AU (1) | AU2012300037B2 (zh) |
BR (1) | BR102012001823B1 (zh) |
WO (1) | WO2013026313A1 (zh) |
ZA (1) | ZA201401646B (zh) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104705555A (zh) * | 2015-04-09 | 2015-06-17 | 裴秀珍 | 一种甘蔗汁制备的焦糖糖浆 |
CN104928403B (zh) * | 2015-04-29 | 2019-05-10 | 广西农垦糖业集团防城精制糖有限公司 | 一种复合石灰乳化剂及其制备方法和应用 |
CN105420418B (zh) * | 2015-11-13 | 2020-03-24 | 南京工业大学 | 一种复合降黏剂及其在糖蜜降黏中的应用 |
KR20170139848A (ko) * | 2016-06-10 | 2017-12-20 | 주식회사 비트윈 | 신기술을 이용한 사탕수수로부터 고순도 원당의 제조방법 |
CN108676926B (zh) * | 2018-06-01 | 2022-04-22 | 广西科技师范学院 | 一种白砂糖的生产方法 |
CN108842007B (zh) * | 2018-06-28 | 2021-09-24 | 广西科技大学 | 一种降低硫熏强度和分离粉末活性炭的工艺方法 |
CN110564795B (zh) * | 2019-09-25 | 2020-05-19 | 泉后(广州)生物科技研究院有限公司 | 大豆多肽及其制备方法和在化妆品中的应用 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1490416A (zh) * | 2003-03-31 | 2004-04-21 | 董超平 | 一种取代亚硫酸法的甘蔗制糖新工艺 |
CN1757756A (zh) * | 2005-08-26 | 2006-04-12 | 张永达 | 蔗汁、糖浆提纯脱色剂及其制备方法和在制糖工艺中的应用 |
CN101144109A (zh) * | 2007-08-15 | 2008-03-19 | 黄桂忠 | 亚硫酸法糖厂混合汁低温处理工艺 |
CN101323885A (zh) * | 2008-07-25 | 2008-12-17 | 高晓军 | 无硫优质蔗糖的生产方法 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60160900A (ja) * | 1984-02-02 | 1985-08-22 | 東洋精糖株式会社 | 不純糖液の処理法 |
GB2221696B (en) * | 1988-07-15 | 1991-10-02 | Itoh Sugar Co Ltd C | Method for refining sugar liquor |
CN1912143A (zh) * | 2005-08-14 | 2007-02-14 | 周少基 | 制糖生产清浊汁分流澄清工艺 |
CN1958811B (zh) * | 2006-07-31 | 2010-05-12 | 广州甘蔗糖业研究所 | 制糖用复合型澄清剂及其制备方法 |
CN101284693B (zh) * | 2008-05-26 | 2010-06-02 | 董超平 | 天然有机高分子复合絮凝剂及其生产方法和应用 |
CN102021250B (zh) * | 2010-12-02 | 2013-11-20 | 杨鲁昆 | 一种糖汁糖浆澄清生产高品质白砂糖的方法 |
-
2011
- 2011-08-24 CN CN201110248232.5A patent/CN102952904B/zh active Active
-
2012
- 2012-01-26 BR BR102012001823-3A patent/BR102012001823B1/pt active IP Right Grant
- 2012-06-15 WO PCT/CN2012/077024 patent/WO2013026313A1/zh active Application Filing
- 2012-06-15 AU AU2012300037A patent/AU2012300037B2/en active Active
-
2014
- 2014-03-05 ZA ZA2014/01646A patent/ZA201401646B/en unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1490416A (zh) * | 2003-03-31 | 2004-04-21 | 董超平 | 一种取代亚硫酸法的甘蔗制糖新工艺 |
CN1757756A (zh) * | 2005-08-26 | 2006-04-12 | 张永达 | 蔗汁、糖浆提纯脱色剂及其制备方法和在制糖工艺中的应用 |
CN101144109A (zh) * | 2007-08-15 | 2008-03-19 | 黄桂忠 | 亚硫酸法糖厂混合汁低温处理工艺 |
CN101323885A (zh) * | 2008-07-25 | 2008-12-17 | 高晓军 | 无硫优质蔗糖的生产方法 |
Also Published As
Publication number | Publication date |
---|---|
AU2012300037A1 (en) | 2014-03-13 |
CN102952904B (zh) | 2014-03-26 |
CN102952904A (zh) | 2013-03-06 |
BR102012001823A2 (pt) | 2016-09-06 |
NZ621417A (en) | 2016-02-26 |
AU2012300037B2 (en) | 2014-07-24 |
BR102012001823B1 (pt) | 2019-10-15 |
ZA201401646B (en) | 2015-03-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2013026313A1 (zh) | 甘蔗制糖新助剂、制备方法及在制糖生产中的应用方法 | |
CN102021250B (zh) | 一种糖汁糖浆澄清生产高品质白砂糖的方法 | |
JP3436540B2 (ja) | テンサイ汁の精製方法 | |
CN102031315B (zh) | 制糖脱色脱钙树脂的再生方法及再生废液的回用方法 | |
EP2499267B1 (en) | Compositions and processes for improving phosphatation clarification of sugar liquors and syrups | |
CN103981290A (zh) | 一种甘蔗制糖工艺 | |
CN103710470A (zh) | 一种二步法制糖的工艺及装置 | |
CN109182609B (zh) | 一种膨润土法甘蔗汁无硫澄清工艺 | |
WO2007017102A1 (en) | Adsorbent and method for purification of crude sugar juices | |
CN108997159B (zh) | 一种l-谷氨酰胺的制备方法 | |
CN112593016A (zh) | 一种由甜菜制取高品质白砂糖和黄腐酸干粉的工艺 | |
CN102161684A (zh) | 一种用混合絮凝剂提取甜叶菊糖的方法 | |
US20200206716A1 (en) | Method for producing functionally improved carbolime | |
WO2017162038A1 (zh) | 植物深加工产品中除钙镁离子的方法 | |
CN110143868B (zh) | 一种柠檬酸钠母液除铁的方法 | |
CN111620776A (zh) | 一种去除柠檬酸钾易炭化物的方法 | |
US20090126720A1 (en) | Sugar cane juice clarification process | |
CN1207212C (zh) | 用糖蜜酒精废液生产钾化工产品的方法 | |
CN106277516B (zh) | 一种甜菊糖生产中吸附废水利用的方法 | |
CN109797249A (zh) | 赤砂糖回溶糖浆的澄清脱色方法 | |
CN117208905B (zh) | 一种用于木糖醇母液脱色工段的活性炭及其制备方法 | |
CN203668420U (zh) | 一种二步法制糖的装置 | |
JPS60160900A (ja) | 不純糖液の処理法 | |
CN105063243A (zh) | 一种糖液的澄清处理方法 | |
JPH04249000A (ja) | 廃糖蜜の清浄法 |
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: 12826264 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: 2012300037 Country of ref document: AU Date of ref document: 20120615 Kind code of ref document: A |
|
32PN | Ep: public notification in the ep bulletin as address of the adressee cannot be established |
Free format text: NOTING OF LOSS OF RIGHTS PURSUANT TO RULE 112(1) EPC (EPO FORM 1205 DATED 24/07/2014) |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 12826264 Country of ref document: EP Kind code of ref document: A1 |