[go: up one dir, main page]

CN101544551A - Method for purifying high-purity organic solvent-acetone for scientific research - Google Patents

Method for purifying high-purity organic solvent-acetone for scientific research Download PDF

Info

Publication number
CN101544551A
CN101544551A CN200910068761A CN200910068761A CN101544551A CN 101544551 A CN101544551 A CN 101544551A CN 200910068761 A CN200910068761 A CN 200910068761A CN 200910068761 A CN200910068761 A CN 200910068761A CN 101544551 A CN101544551 A CN 101544551A
Authority
CN
China
Prior art keywords
acetone
organic solvent
scientific research
purification
purity
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
CN200910068761A
Other languages
Chinese (zh)
Inventor
宋金链
张玉芝
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.)
National Institute of Metrology
Original Assignee
Tianjin Concord Technology 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 Tianjin Concord Technology Co Ltd filed Critical Tianjin Concord Technology Co Ltd
Priority to CN200910068761A priority Critical patent/CN101544551A/en
Publication of CN101544551A publication Critical patent/CN101544551A/en
Pending legal-status Critical Current

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Treatment Of Liquids With Adsorbents In General (AREA)

Abstract

The invention relates to a method for purifying a high-purity organic solvent-acetone for scientific research, which comprises the following steps that: acetone as the raw material is adsorbed to remove impurities by an adsorption resin, dried to remove water by a drying agent, rectified by a rectifying still, filtered and packaged to obtain a chromatographic grade and pesticide residue grade acetone product. The method can obtain the chromatographic acetone product with the purity more than 99.9 percent, ensure that the yield is more than 93 percent and the qualification rate is more than 95 percent, can obtain a 50 to 60 percent pesticide residue grade acetone reagent, can meet the application demand of high efficiency liquid chromatography (HPLC) customers on pesticide residue, and fill in the gap of the national production of pesticide residue grade chromatography reagents; and at the same time, compared with the prior method, the method has high product purity, simple and convenient operation and stable operation, and is suitable for mass production.

Description

一种科研用高纯有机溶剂丙酮的提纯方法 A kind of purification method of high-purity organic solvent acetone for scientific research

技术领域 technical field

本发明属于化工技术领域,涉及有机溶剂的提纯方法,尤其是一种科研用高纯有机溶剂丙酮的提纯方法。The invention belongs to the technical field of chemical industry and relates to a method for purifying an organic solvent, in particular to a method for purifying acetone, a high-purity organic solvent used in scientific research.

背景技术 Background technique

市面上销售的丙酮试剂,其丙酮含量约99.5%,其中含有少量不饱和烃类、水等杂质。此种丙酮并不能满足相关科研试验的需要,因此该种丙酮必须经过进一步纯化,使其各项技术指标都达到色谱级、农残级丙酮的标准才能使用。The acetone reagent sold on the market has an acetone content of about 99.5%, which contains a small amount of unsaturated hydrocarbons, water and other impurities. This kind of acetone cannot meet the needs of relevant scientific research experiments, so this kind of acetone must be further purified so that its various technical indicators can reach the standards of chromatographic grade and pesticide residue grade acetone before it can be used.

目前,国内关于丙酮纯化方面的资料,大多集中于废液中丙酮的回收利用,其中专利号分别为:200710028462.4、200710060107.5中分别就废液中丙酮的回收提供了相关的方法和装置,但不适用于高纯度丙酮(含量99.5%)的提纯。At present, domestic information on acetone purification mostly focuses on the recovery and utilization of acetone in waste liquid. The patent numbers are: 200710028462.4 and 200710060107.5 respectively provide related methods and devices for the recovery of acetone in waste liquid, but they are not applicable In the purification of high-purity acetone (content 99.5%).

据检索,国内关于高纯度丙酮试剂的进一步提纯方法相关阐述甚少,主要是由于经过初步提纯的丙酮中杂质的含量少,精馏中很难将杂质除去,因此,本发明是针对这一技术难题提出有效的解决方法。According to the search, there are very few related elaborations on further purification methods of high-purity acetone reagents in China, mainly because the content of impurities in acetone through preliminary purification is small, and it is difficult to remove impurities in rectification. Therefore, the present invention is aimed at this technology. Problems come up with effective solutions.

发明内容 Contents of the invention

本发明的目的是提供一种科研用高纯有机溶剂丙酮的提纯方法,该提纯方法具有工艺简单、残渣易分离、产品纯度高等特点。The object of the present invention is to provide a method for purifying acetone, a high-purity organic solvent for scientific research, which has the characteristics of simple process, easy separation of residues, and high product purity.

本发明是通过以下方案实施的:The present invention is implemented through the following scheme:

一种科研用高纯有机溶剂丙酮的提纯方法,提纯的步骤如下:A kind of purification method of high-purity organic solvent acetone for scientific research, the step of purification is as follows:

(1)将原料丙酮通过吸附树脂柱以除去杂质;(1) the raw material acetone is passed through the adsorption resin column to remove impurities;

(2)将吸附后的丙酮进行干燥,并测定含水量;(2) dry the acetone after adsorption, and measure the water content;

(3)将干燥后含水量在合格范围的丙酮进行精馏,精馏后过滤,即得到色谱级和农残级丙酮产品。(3) Carry out rectification to the acetone with moisture content in the acceptable range after drying, and filter after rectification to obtain chromatographic grade and pesticide residue grade acetone products.

而且,所述的吸附树脂为Amberlite XAD-4,干燥剂为无水硫酸钾或无水碳酸钾。Moreover, the adsorption resin is Amberlite XAD-4, and the desiccant is anhydrous potassium sulfate or anhydrous potassium carbonate.

而且,所述的原料丙酮以20-80mL/min速度流经吸附树脂柱。Moreover, the raw material acetone flows through the adsorption resin column at a speed of 20-80mL/min.

而且,所述的步骤(3)中丙酮中合格含水量范围控制在≤0.2%。Moreover, the qualified water content range in the acetone in the step (3) is controlled at ≤0.2%.

而且,所述将干燥后的丙酮进行精馏的条件为:精馏釜底温度100~300℃,釜中丙酮液体温度61℃~65℃,釜顶温度55℃~57℃,控制回流比1∶3~5。Moreover, the conditions for rectifying the dried acetone are as follows: the temperature at the bottom of the rectification tank is 100-300°C, the temperature of the acetone liquid in the tank is 61-65°C, the temperature at the top of the tank is 55-57°C, and the reflux ratio is controlled at 1 : 3~5.

本发明的优点和积极效果是:Advantage and positive effect of the present invention are:

1、本发明以含量为99.5%的丙酮为原料、以吸附树脂作为吸附剂进行吸附分离除去其中的杂质,采用无水硫酸钾或无水碳酸钾作为干燥剂除去其中的水分,经过吸附、干燥、精馏提纯得到纯度99.9%的丙酮产品,该提纯方法简单,残渣易分离,产品纯度高,运行稳定,适于规模化生产。1. The present invention uses acetone with a content of 99.5% as a raw material, uses an adsorption resin as an adsorbent to carry out adsorption and separation to remove impurities therein, uses anhydrous potassium sulfate or anhydrous potassium carbonate as a desiccant to remove moisture therein, and undergoes adsorption and drying. 1. The acetone product with a purity of 99.9% is obtained by rectification and purification. The purification method is simple, the residue is easy to separate, the product has high purity, stable operation, and is suitable for large-scale production.

2、本提纯方法用吸附树脂进行吸附去除丙酮中的杂质,提升丙酮含量至99.9%,其它各项指标都达到色谱级要求,成品率由原来的70%提高至90%,节省了人力,减少了能源的消耗,更适用于工业化的生产和应用,具有显著的经济效益。2. This purification method uses adsorption resin to absorb and remove impurities in acetone, and the content of acetone is increased to 99.9%. It reduces energy consumption, is more suitable for industrial production and application, and has significant economic benefits.

3、本提纯方法生产的产品经检测其各项指标符合色谱级、农残级色谱丙酮的要求,其丙酮含量大于99.9%,回收率大于93%,成品率达到95%,其中可得到50-60%的农残级丙酮试剂,该产品可以满足高效液相色谱(HPLC)的客户在农药残留中的应用需求,填补了国内农残级试剂生产的空白。3, the product produced by this purification method meets the requirements of chromatographic grade and pesticide residue grade chromatographic acetone after testing its various indicators, its acetone content is greater than 99.9%, the recovery rate is greater than 93%, and the yield of finished product reaches 95%, wherein 50- 60% pesticide residue-grade acetone reagent, this product can meet the application needs of high-performance liquid chromatography (HPLC) customers in pesticide residues, and fills the gap in the domestic production of pesticide residue-grade reagents.

具体实施例 specific embodiment

下面通过具体实施例对本发明作进一步详述,以下实施例只是描述性的,不是限定性的,不能以此限定本发明的保护范围。The present invention will be further described in detail below through the specific examples, the following examples are only descriptive, not restrictive, and cannot limit the protection scope of the present invention with this.

实施例1:Example 1:

一种科研用高纯有机溶剂丙酮的提纯方法,步骤如下:A kind of purification method of high-purity organic solvent acetone for scientific research, the steps are as follows:

(1)将原料丙酮(含量约为99.5%)提升至吸附塔上方,其中吸附塔高2M,直径10cm,内装吸附树脂的量为塔高的4/5,丙酮原料以20mL/min速度进行吸附;在塔内,丙酮与吸附树脂充分接触,使不饱和烃类杂质被吸附掉,检测吸附出液质量,待吸附出液检验合格(即流出液各项指标接近色谱级和农残级的技术指标要求,其具体技术指标要求见表1)后,进入下步操作,并将杂质高的吸附前馏分除去。(1) Lift the raw acetone (content is about 99.5%) above the adsorption tower, wherein the adsorption tower is 2M high, 10cm in diameter, and the amount of adsorption resin inside is 4/5 of the tower height, and the acetone raw material is adsorbed at a speed of 20mL/min ; In the tower, acetone is fully contacted with the adsorption resin, so that the unsaturated hydrocarbon impurities are adsorbed, and the quality of the adsorbed liquid is detected, and the quality of the adsorbed liquid is tested to be qualified (that is, the indicators of the effluent are close to the chromatographic level and the technology of the pesticide residue level. Index requirements, its specific technical index requirements are shown in Table 1), enter the next step operation, and remove the fraction before adsorption with high impurity.

(2)将上述吸附塔流出的丙酮进入干燥塔,塔高2M,直径10cm,装入经烘烤干燥的无水硫酸钾,测量干燥后丙酮的含水量,水分控制在≤0.2%,含水量合格后进入下步操作;如果水分含量大于0.25%时,说明干燥剂已经被水饱和,必须更换之后再进行干燥处理。(2) The acetone flowing out of the above-mentioned adsorption tower enters the drying tower, the tower height is 2M, and the diameter is 10cm, and the anhydrous potassium sulfate through baking and drying is loaded into, and the water content of the acetone after measurement is dried, and the moisture is controlled at ≤0.2%. Enter the next step after passing the test; if the moisture content is greater than 0.25%, it means that the desiccant has been saturated with water and must be replaced before drying.

(3)将上述经干燥后的丙酮注入100L的不锈钢精馏釜进行精馏,利用导热油加热,控制不锈钢釜底温度100℃,釜中丙酮液体温度61℃,出液温度55℃,控制回流比在1:3出液,成品经0.45μmNYL微孔滤膜过滤后,在氮气保护下装瓶密封,即取得合格的色谱级、农残级丙酮产品(纯度99.9%),其前馏分作进一步处理。(3) Pour the above-mentioned dried acetone into a 100L stainless steel rectification kettle for rectification, use heat conduction oil to heat, control the bottom temperature of the stainless steel kettle to 100°C, the temperature of the acetone liquid in the kettle to 61°C, the temperature of the liquid out to 55°C, and control the reflux The liquid is discharged at a ratio of 1:3, and the finished product is filtered through a 0.45 μm NYL microporous membrane, bottled and sealed under nitrogen protection, and a qualified chromatographic grade and pesticide residue grade acetone product (purity 99.9%) is obtained. deal with.

实施例2:Example 2:

一种科研用高纯有机溶剂丙酮的提纯方法,步骤如下:A kind of purification method of high-purity organic solvent acetone for scientific research, the steps are as follows:

(1)将原料丙酮(含量约为99.5%)提升至吸附塔上方,吸附塔高2M,直径10cm,内装吸附树脂的量为塔高的4/5,丙酮原料以80mL/min速度进行吸附,吸附出液检验合格后进入下步操作;并将杂质高的吸附前馏分除去。(1) The raw material acetone (content is about 99.5%) is lifted above the adsorption tower, the adsorption tower is 2M high, the diameter is 10cm, the amount of built-in adsorption resin is 4/5 of the tower height, and the acetone raw material is adsorbed at a speed of 80mL/min, After the adsorption effluent is qualified, enter the next step of operation; and remove the fraction with high impurities before adsorption.

(2)将上述吸附塔的流出液进入干燥塔,塔高2M,直径10cm,装入经烘烤干燥的无水碳酸钾,测量干燥后丙酮的含水量,水分控制在≤0.2%,含水量合格后进入下步操作;当水分含量大于0.25%时,说明干燥剂已经被水饱和,必须更换之后再进行干燥处理。(2) The effluent of the above-mentioned adsorption tower is entered into the drying tower, the tower height is 2M, and the diameter is 10cm, and the anhydrous potassium carbonate through baking and drying is packed into, and the moisture content of the acetone after measurement is dried, and the moisture content is controlled at ≤0.2%. Enter the next step after passing the test; when the moisture content is greater than 0.25%, it means that the desiccant has been saturated with water and must be replaced before drying.

(3)将上述经干燥后丙酮注入120L的不锈钢精馏釜进行精馏。利用导热油加热,控制不锈钢釜底温度300℃,釜中丙酮液体温度65℃,出液温度57℃,控制回流比在1∶5出液,成品经0.45μmNYL微孔滤膜过滤后,在氮气保护下装瓶密封,即取得合格的色谱级、农残级丙酮产品(纯度99.9%);其前馏分作进一步处理。(3) The above-mentioned dried acetone is injected into a 120L stainless steel distillation still for rectification. Use heat conduction oil to heat, control the temperature at the bottom of the stainless steel kettle to 300°C, the temperature of the acetone liquid in the kettle to 65°C, and the liquid outlet temperature to 57°C, and control the reflux ratio to 1:5. Bottling under protection is sealed to obtain qualified chromatographic grade and pesticide residue grade acetone products (purity 99.9%); the preceding fraction is further processed.

农残级指标的测定:Determination of pesticide residue level indicators:

农残级指标:样品除满足色谱级指标外,浓缩300倍后,用GC-ECD气相色谱仪检测到的所有杂峰(与γ-六六六峰高比较)均低于10ng/L,农残级为合格。这样经过纯化过的高纯丙酮,经过进一步提纯可得到50-60%的农残级色谱丙酮产品。Pesticide level indicators: In addition to meeting the chromatographic level indicators, after the sample is concentrated 300 times, all the miscellaneous peaks detected by GC-ECD gas chromatography (compared with the peak height of γ-HCH) are all lower than 10ng/L, and the pesticide Residual grade is qualified. The purified high-purity acetone can be further purified to obtain 50-60% pesticide residue grade chromatographic acetone product.

表1:原料、色谱、农残级丙酮的技术指标Table 1: Technical indicators of raw materials, chromatography, and pesticide residue grade acetone

Figure A200910068761D00051
Figure A200910068761D00051

Claims (5)

1, a kind of method of purification of high-purity organic solvent-acetone for scientific research is characterized in that: the step of purification is as follows:
(1) with raw material acetone by adsorption resin column to remove impurity;
(2) acetone after will adsorbing carries out drying, and measures water content;
(3) water content after the drying is carried out rectifying at the acetone of acceptability limit, the rectifying after-filtration promptly obtains chromatographic grade and pesticide-residue-level acetone product.
2, the method for purification of a kind of high-purity organic solvent-acetone for scientific research according to claim 1 is characterized in that: described polymeric adsorbent is Amberlite XAD-4, and siccative is anhydrous potassium sulfate or Anhydrous potassium carbonate.
3, the method for purification of a kind of high-purity organic solvent-acetone for scientific research according to claim 1 is characterized in that: described raw material acetone with the 20-80mL/min velocity flow through adsorption resin column.
4, the method for purification of a kind of high-purity organic solvent-acetone for scientific research according to claim 1 is characterized in that: in the described step (3) in the acetone qualified water content ranges be controlled at≤0.2%.
5, the method for purification of a kind of high-purity organic solvent-acetone for scientific research according to claim 1, it is characterized in that: the described condition that dried acetone is carried out rectifying is: temperature is 100~300 ℃ at the bottom of the rectifying still, the acetone fluid temperature is 61 ℃~65 ℃ in the still, 55 ℃~57 ℃ of still top temperature, control reflux ratio 1:3~5.
CN200910068761A 2009-05-06 2009-05-06 Method for purifying high-purity organic solvent-acetone for scientific research Pending CN101544551A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200910068761A CN101544551A (en) 2009-05-06 2009-05-06 Method for purifying high-purity organic solvent-acetone for scientific research

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200910068761A CN101544551A (en) 2009-05-06 2009-05-06 Method for purifying high-purity organic solvent-acetone for scientific research

Publications (1)

Publication Number Publication Date
CN101544551A true CN101544551A (en) 2009-09-30

Family

ID=41191955

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200910068761A Pending CN101544551A (en) 2009-05-06 2009-05-06 Method for purifying high-purity organic solvent-acetone for scientific research

Country Status (1)

Country Link
CN (1) CN101544551A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101759537A (en) * 2010-01-28 2010-06-30 安徽时联特种溶剂股份有限公司 Method for producing HPLC-grade acetone
CN101973859A (en) * 2010-10-29 2011-02-16 上海化学试剂研究所 Method and device for preparing ultrapure acetone
CN102040497A (en) * 2010-12-29 2011-05-04 天津市康科德科技有限公司 Purification method of high-purity organic solvent butanone
CN102040496A (en) * 2010-12-29 2011-05-04 天津市康科德科技有限公司 Purification method of high-purity organic solvent 4-methyl-2-pentanone
CN102329200A (en) * 2011-07-19 2012-01-25 天津基准化学试剂有限公司 Method for preparing high-voltage electrophoresis reagent acetone
CN102417441A (en) * 2011-12-26 2012-04-18 天津市康科德科技有限公司 Purification method of chromatographic grade organic solvent methyl tert-butyl ether
CN102452892A (en) * 2010-10-15 2012-05-16 中国石油化工股份有限公司 Method for purifying pesticide residue grade dichloromethane for extraction
CN104119216A (en) * 2014-08-01 2014-10-29 苏州市晶协高新电子材料有限公司 Production method of continuous acetone dehydration
CN105175236A (en) * 2015-09-25 2015-12-23 江阴润玛电子材料股份有限公司 Ultra-clean high-purity acetone production method
CN113321576A (en) * 2021-05-31 2021-08-31 成都市科隆化学品有限公司 Benzene-free acetone and preparation method thereof

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101759537A (en) * 2010-01-28 2010-06-30 安徽时联特种溶剂股份有限公司 Method for producing HPLC-grade acetone
CN101759537B (en) * 2010-01-28 2014-06-18 安徽时联特种溶剂股份有限公司 Method for producing HPLC-grade acetone
CN102452892A (en) * 2010-10-15 2012-05-16 中国石油化工股份有限公司 Method for purifying pesticide residue grade dichloromethane for extraction
CN101973859A (en) * 2010-10-29 2011-02-16 上海化学试剂研究所 Method and device for preparing ultrapure acetone
CN101973859B (en) * 2010-10-29 2014-12-31 上海化学试剂研究所 Method and device for preparing ultrapure acetone
CN102040496A (en) * 2010-12-29 2011-05-04 天津市康科德科技有限公司 Purification method of high-purity organic solvent 4-methyl-2-pentanone
CN102040497A (en) * 2010-12-29 2011-05-04 天津市康科德科技有限公司 Purification method of high-purity organic solvent butanone
CN102329200B (en) * 2011-07-19 2013-08-14 天津基准化学试剂有限公司 Method for preparing high-voltage electrophoresis reagent acetone
CN102329200A (en) * 2011-07-19 2012-01-25 天津基准化学试剂有限公司 Method for preparing high-voltage electrophoresis reagent acetone
CN102417441A (en) * 2011-12-26 2012-04-18 天津市康科德科技有限公司 Purification method of chromatographic grade organic solvent methyl tert-butyl ether
CN104119216A (en) * 2014-08-01 2014-10-29 苏州市晶协高新电子材料有限公司 Production method of continuous acetone dehydration
CN104119216B (en) * 2014-08-01 2016-02-24 苏州市晶协高新电子材料有限公司 A kind of production method of acetone serialization dehydration
CN105175236A (en) * 2015-09-25 2015-12-23 江阴润玛电子材料股份有限公司 Ultra-clean high-purity acetone production method
CN113321576A (en) * 2021-05-31 2021-08-31 成都市科隆化学品有限公司 Benzene-free acetone and preparation method thereof
CN113321576B (en) * 2021-05-31 2023-06-13 成都市科隆化学品有限公司 Non-propiophenone and preparation method thereof

Similar Documents

Publication Publication Date Title
CN101544551A (en) Method for purifying high-purity organic solvent-acetone for scientific research
CN101544531B (en) Method for purifying high-purity organic solvent-normal hexane for scientific research
CN101570468B (en) Method for preparing pesticide residue grade chromatographic ethanol
CN102040455A (en) Purification method of chromatographically pure organic solvent cyclohexane
CN101723922B (en) Method for purifying high-purity organic solvent tetrahydrofuran for scientific research
CN101570484A (en) Method for preparing pesticide residue grade chromatographic ethyl acetate
CN102432499A (en) Purification method of high performance liquid chromatography eluent acetonitrile
CN104072388B (en) Preparation method for high-purity gradient acetonitrile
CN103342626B (en) Preparation method of chromatographic grade methanol
CN102417441A (en) Purification method of chromatographic grade organic solvent methyl tert-butyl ether
CN102093160B (en) Method for preparing chromatographically-pure trichloromethane
CN102320623A (en) Purification device and purification method for electronic grade ultra-pure ammonia
CN102060674B (en) Method for purifying high-purity organic solvent diethyl ether
CN102115356A (en) Method for preparing chromatograph-grade normal heptane
CN102040583A (en) Method for preparing high-purity liquid-phase chromatographic grade 1,4-dioxane
Kupiec et al. Heat and mass transfer in adsorption–desorption cyclic process for ethanol dehydration
CN102060650A (en) Method for purifying chromatographic grade toluene
CN102070393A (en) Preparation method of high-efficiency liquid chromatographic-grade cyclohexane
CN102432428A (en) Method for purifying chromatographically pure organic solvent tert-butyl alcohol
CN102746115A (en) Purification method for high-purity organic solvent normal propyl alcohol
CN102040496A (en) Purification method of high-purity organic solvent 4-methyl-2-pentanone
CN102731248A (en) Purification method of highly pure organic solvent n-propanol
CN107522678A (en) A kind of chromatogram pure tetrahydrofuran and preparation method thereof, production system
CN102040497A (en) Purification method of high-purity organic solvent butanone
CN210855273U (en) Purification device of high-purity hydrogen sulfide

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20100108

Address after: Tianjin City, Hebei District Yu Guan Road No. 15 post encoding: 300230

Applicant after: Tianjin Concord science and Technology Co., Ltd.

Co-applicant after: National Institute of Metrology, China

Address before: Tianjin City, Hebei District Yu Guan Road No. 15 post encoding: 300230

Applicant before: Tianjin Concord Technology Co., Ltd.

C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20090930