CN107446979A - A kind of method of two steps enzymolysis and extraction wheat bran albumen - Google Patents

A kind of method of two steps enzymolysis and extraction wheat bran albumen Download PDF

Info

Publication number
CN107446979A
CN107446979A CN201710851711.3A CN201710851711A CN107446979A CN 107446979 A CN107446979 A CN 107446979A CN 201710851711 A CN201710851711 A CN 201710851711A CN 107446979 A CN107446979 A CN 107446979A
Authority
CN
China
Prior art keywords
wheat bran
albumen
extraction
temperature
concentration
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
CN201710851711.3A
Other languages
Chinese (zh)
Inventor
王建勋
侯同刚
咸漠
王乔
董晴晴
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.)
Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Original Assignee
Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
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 Qingdao Institute of Bioenergy and Bioprocess Technology of CAS filed Critical Qingdao Institute of Bioenergy and Bioprocess Technology of CAS
Priority to CN201710851711.3A priority Critical patent/CN107446979A/en
Publication of CN107446979A publication Critical patent/CN107446979A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P21/00Preparation of peptides or proteins
    • C12P21/06Preparation of peptides or proteins produced by the hydrolysis of a peptide bond, e.g. hydrolysate products

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Zoology (AREA)
  • Engineering & Computer Science (AREA)
  • Wood Science & Technology (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Biotechnology (AREA)
  • Molecular Biology (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

The invention discloses a kind of method of two steps enzymolysis and extraction wheat bran albumen, it is related to bioengineering field.Methods described takes wheat bran slag including (1), adds distilled water and sizes mixing, adjusts pH and temperature, adds breaking-wall cell enzyme reaction and obtains by pretreated slurry;(2) obtained slurry is directly added into distilled water re-started and size mixing, adjust pH and temperature, without other processing, after adding basic protein enzyme reaction 1h 6h, centrifuge, take supernatant and be freeze-dried, you can obtain protein product.Other Enzymatic Extractions are compared, and this method can sufficiently improve the recovery rate of rice bran protein.And especially suitable for the wheat bran after high-temperature process.

Description

A kind of method of two steps enzymolysis and extraction wheat bran albumen
Technical field
The present invention relates to bioengineering field, more particularly to a kind of extracting method of wheat bran albumen, more particularly to one kind The method that two step enzymatic isolation methods extract wheat bran albumen.
Background technology
Accessory substance of the wheat bran as milling industry, annual production are very abundant and cheap.From the point of view of plant histology, Wheat bran is made up of successively pericarp, kind skin, megarchidium layer and aleurone.And completely can not be separated wheat bran layer during Flour production, So also contain plumule and endosperm layer except the cortex containing wheat in wheat bran.Thus, generally, contain in wheat bran 12% moisture, 13% albumen, 4% fat and 45% dietary fiber and some other carbohydrate.
For wheat gluten, the albumen in wheat bran contains higher proportion of lysine, arginine, alanine, day Winter propylhomoserin and glycine and less glutamine, proline, the amino acid of phenylalanine and some sulfur-bearings.Thus, wheat Albumen in bran has higher nutritive value, can be added in food and some special feeds and improve nutriture value Value;Wheat bran albumen also has good emulsibility, can apply it in baking goodses and soup stock;Wheat bran albumen is by enzymolysis Obtained polypeptide can be used as anti-oxidation peptide and antifatigue peptide afterwards;In addition, wheat bran albumen also has freeze proof performance, It can be added to as the antifreeze of food in food to ensure quality of the food in cryopreservation.
Both at home and abroad extraction wheat bran protein main method for chemical leaching test, Enzymatic Extraction method, ethanol extraction method and Salt extraction method etc..Chemical leaching test is exactly alkaline extraction, and wheat bran passes through certain under the conditions of alkalescence condition and certain temperature Centrifuge after time and obtain supernatant, regulation pH to isoelectric point, through centrifugation can obtain sediment you, regulation precipitation For pH to neutral and then after freeze-drying can obtain wheat bran albumen.Alkalinity extraction is simple to operate, is easier to control Process conditions processed, extraction efficiency is also higher, thus is applied to large-scale industrial production, but for after High-temperature Liquefaction For wheat bran slag, because albuminous degeneration is serious, thus it is relatively low with alkalinity extraction rate;Enzymatic Extraction mainly uses protease, Because protease can be modified and some vegetable proteins of degrading obtain the soluble protein and soluble peptide of some small molecules, and And enzyme extraction reaction condition is gentle, accessory substance is less, is a kind of method of the current production high-quality protein generally used;Extraction carries Follow the example of protein in Shi Liyong alcohol steep wheat brans, the impurity contained by the protein of this method extraction is relatively more and extraction process Cost is higher, thus is not suitable for producing on a large scale.
The content of the invention
For problem present in above-mentioned existing technology, it is an object of the invention to provide a kind of two step enzymolysis and extraction wheats The method of gliadin, this method is simple to operate, reproducible, can greatly improve the recovery rate and purity of wheat bran albumen.
According to a kind of method of two steps enzymolysis and extraction wheat bran albumen of the present invention, described method comprises the following steps:
(1) the wheat bran slag after removing except starch, adding deionized water and sizing mixing makes wine with dregs concentration in 10%-30%, with quality point Number adjusts slurry pH to 4.0-7.0 for 5% hydrochloric acid, while adjusts slurry temperature as 40-70 DEG C, total matter based on wheat bran slag Amount adds Broken kernel enzyme, and Broken kernel enzyme adds the 0.03%-0.3% that quality is wheat bran slag gross mass, after reacting 0.5-5h Obtain the wheat bran slurry by pretreatment;
(2) add distilled water in the wheat bran slurry by pretreatment obtained to step (1) and size mixing again and be to wine with dregs concentration 4%-25%, and Ph to 6.0-10.0 is adjusted with the sodium hydroxide solution that mass concentration is 4%, it is 55-100 by temperature adjustment DEG C, alkali protease is added based on wheat bran gross weight, adds the 1.0-3.0% that quality is wheat bran gross weight, reaction 1-5h is laggard Row centrifuges, and described centrifugal rotational speed is 2000-5000rpm, is freeze-dried after taking supernatant concentration, you can obtain wheat bran Protein product.
Preferably, the wine with dregs concentration after sizing mixing described in step (1) is 15%;Described pH is 5.5;Described temperature For 50 DEG C;Described Broken kernel enzyme is the Viscozyme L that Novi believes preparation Co., Ltd, the enzyme amount added be based on The 0.2% of wheat bran gross weight;The described reaction time is 2.5h.
Preferably, the wine with dregs concentration sized mixing again described in step (2) is 10%;Described pH is 8.0;Described temperature Spend for 80 DEG C, described alkali protease believes the Alcalase 2.4L FG of preparation Co., Ltd, the enzyme amount added for Novi For the 2.0% of wheat bran gross weight;Reaction time is 2h, and described centrifugal rotational speed is 4000rpm.
The slurry that the step 1) obtains is handled without other, is directly used in step 2).
The reactants such as alkali or acid need not be added in methods described to be reacted, the alkali includes inorganic base or organic base, institute Stating acid includes inorganic acid or organic acid.
Above-mentioned " the wheat bran slag after removing except starch " is to add α-amylase liquefaction after being heated to 85-110 DEG C after wheat bran is sized mixing, And the product obtained after filtering, because the process temperature is higher, the wheat bran slag because obtained from is the wheat after high-temperature process Bran, this process can remove most of starch in wheat bran.
Beneficial effect
Compared with conventional method, Enzymatic Extraction makes insoluble or albuminate become soluble peptide to be dissolved out, by egg The polypeptide chain of white matter is hydrolyzed into short peptide chain, improves the digestibility of protein, while reduces the concentration of substrate of reactant, saves The consumption of alkali and water, the content of solid content in extract solution is improved, remove the energy of extract solution moisture so as to reduce and disappear Consumption, condition is created for industrial production.
According to the present invention two step enzymolysis and extraction wheat bran methods compared with other Enzymatic Extractions, this method especially suitable for Wheat bran after high-temperature process because high temperature causes the albuminous degeneration in wheat bran, traditional enzyme process and chemical method be difficult by Protein extraction therein comes out.The present invention first uses Broken kernel enzyme by the cell of wheat bran before protease extracts wheat bran albumen Wall is crushed, and is that protein molecular fully exposes, is reused alkali protease and albumen therein is degraded, becoming it can The polypeptide of dissolubility or small protein molecular, this method can not only increase the recovery rate of wheat bran albumen, and can be modified Albumen through being denatured, increase its dissolubility.Two enzymes method extracts the industrial biomass high-temperature albuminate of method of wheat bran albumen Extraction established inositol.
Embodiment
Hereinafter, it will be described in detail the present invention.Before doing so, it should be appreciated that in this specification and appended Claims in the term that uses should not be construed as being limited to general sense and dictionary meanings, and inventor should allowed On the basis of appropriate definition term is to carry out the principle of best interpretations, according to implication corresponding with the technical elements of the present invention and generally Thought explains.Therefore, description presented herein is not intended to limitation originally merely for the sake of the preferred embodiment for illustrating purpose The scope of invention, it will thus be appreciated that without departing from the spirit and scope of the present invention, it can be obtained by it His equivalents or improved procedure.
Following examples are enumerated only as the example of embodiment of the present invention, do not form any limit to the present invention System, it will be appreciated by those skilled in the art that the modification in the range of without departing from the essence of the present invention and design each falls within the present invention Protection domain.Unless otherwise indicated, the reactant used in following examples is commercially available prod.
Embodiment 1
(1) the wheat bran slag after removing except starch, adding deionized water and sizing mixing makes the wine with dregs concentration be with mass fraction 15% 5% hydrochloric acid regulation slurry pH to 5.5 and temperature is 50 DEG C, and the gross mass based on wheat bran slag adds Broken kernel enzyme, is included in Measure as 0.2%, the wheat bran slurry by pretreatment is obtained after reacting 2h.
(2) it is 10% that distilled water is added in the slurry for obtaining step (1) to step (1) and is sized mixing again to wine with dregs concentration, and PH to 8.0 is adjusted with the sodium hydroxide solution that mass concentration is 4%, temperature is set as 80 DEG C, added based on wheat bran gross weight The Alcalase 2.4L FG of letter preparation Co., Ltd of Novi, addition 2.0%, are centrifuged after reaction 2, described Centrifugal rotational speed is 4000rpm.It is freeze-dried after taking supernatant concentration, you can obtain wheat bran protein product.
Embodiment 2
In addition to the wine with dregs concentration in step (1) is arranged into 10%.Wheat bran is extracted according to identical method in embodiment 1 Albumen.As a result as shown in table 1, the protein extracting ratio of step (1) is 3%.
Embodiment 3
In addition to the wine with dregs concentration in step (1) is arranged into 20%.Wheat bran is extracted according to identical method in embodiment 1 Albumen.As a result as shown in table 1, the protein extracting ratio of step (1) is 4.7%
Embodiment 4
In addition to the wine with dregs concentration in step (1) is arranged into 25%.Wheat bran is extracted according to identical method in embodiment 1 Albumen.As a result as shown in table 1, the protein extracting ratio of step (1) is 4.1%
Embodiment 5
In addition to the wine with dregs concentration in step (1) is arranged into 30%.Wheat bran is extracted according to identical method in embodiment 1 Albumen.As a result as shown in table 1, the protein extracting ratio of step (1) is 2.6%
It can be seen that the wine with dregs concentration in step (1) has direct shadow to the protein extracting ratio of composite fibre enzyme from the data of table 1 Ring, when wine with dregs concentration is 15%, protein extracting ratio highest, now the hydrolysis result of Broken kernel enzyme is best.
Embodiment 6
Except by addition to temperature is arranged to 55 DEG C in step (2), wheat bran egg is extracted according to identical method in embodiment 1 In vain.As a result as shown in table 2, the protein extracting ratio of step (2) is 32%.
Embodiment 7
Except by addition to temperature is arranged to 65 DEG C in step (2), wheat bran egg is extracted according to identical method in embodiment 1 In vain.As a result as shown in table 2, the protein extracting ratio of step (2) is 41%.
Embodiment 8
Except by addition to temperature is arranged to 75 DEG C in step (2), wheat bran egg is extracted according to identical method in embodiment 1 In vain.As a result as shown in table 2, the protein extracting ratio of step (2) is 45%.
Embodiment 9
Except by addition to temperature is arranged to 85 DEG C in step (2), wheat bran egg is extracted according to identical method in embodiment 1 In vain.As a result as shown in table 2, the protein extracting ratio of step (2) is 64%.
Embodiment 10
Except by addition to temperature is arranged to 90 DEG C in step (2), wheat bran egg is extracted according to identical method in embodiment 1 In vain.As a result as shown in table 2, the protein extracting ratio of step (2) is 62%.
Wine with dregs concentration Protein extracting ratio
Embodiment 2 3%
Embodiment 1 5.2%
Embodiment 3 4.7%
Embodiment 4 4.1%
Embodiment 5 2.6%
Table 1
Table 2
pH Protein extracting ratio
Embodiment 11 14%
Embodiment 12 28%
Embodiment 1 71%
Embodiment 13 62%
Embodiment 14 52%
Table 3
Embodiment 11
Except by addition to pH is arranged to 6.0 in step (2), wheat bran albumen is extracted according to identical method in embodiment 1.Knot Fruit is as shown in table 3, and the protein extracting ratio of step (2) is 14%.
Embodiment 12
Except by addition to pH is arranged to 7.0 in step (2), wheat bran albumen is extracted according to identical method in embodiment 1.Knot Fruit is as shown in table 3, and the protein extracting ratio of step (2) is 28%.
Embodiment 13
Except by addition to pH is arranged to 9.0 in step (2), wheat bran albumen is extracted according to identical method in embodiment 1.Knot Fruit is as shown in table 3, and the protein extracting ratio of step (2) is 62%.
Embodiment 14
Except by addition to pH is arranged to 10.0 in step (2), wheat bran albumen is extracted according to identical method in embodiment 1. As a result as shown in table 3, the protein extracting ratio of step (2) is 52%.Comparative example 1
In addition to the raw material in step (1) to be replaced by the wheat bran of unprocessed (without except starch i.e. high-temperature process). Wheat bran albumen is extracted according to the identical method of embodiment 1.The recovery rate of albumen is 82%.Above-mentioned conclusion proves that this method is handled The ability of wheat bran without high-temperature process is more or less the same with handling the ability of the wheat bran through high-temperature process.
Comparative example 2
Remove except the wheat bran slag after starch, adding deionized water and sizing mixing makes wine with dregs concentration 15%, and is 4% with mass concentration Sodium hydroxide solution regulation pH to 1.0, temperature is set as 80 DEG C, is centrifuged after reacting 1h, described centrifugation turns Speed is 4000rpm.It is freeze-dried after taking supernatant concentration, you can obtain wheat bran protein product, the recovery rate of albumen is 25%.On Stating result proves:Except the wheat bran slag after starch (i.e. by high-temperature process), the recovery rate that albumen is extracted with this method is tradition side Nearly 3 times of method recovery rate, this is the change of very big amount, be those skilled in the art learn technical scheme and It is difficult to what is expected before its technique effect.

Claims (5)

1. a kind of method of albumen in two steps enzymolysis and extraction wheat bran, it is characterised in that:Comprise the following steps:
(1) the wheat bran slag after removing except starch, adding deionized water and sizing mixing makes the wine with dregs concentration be with mass fraction in 10%-30% 5% hydrochloric acid adjusts slurry pH to 4.0-7.0, while adjusts slurry temperature as 40-70 DEG C, and the gross mass based on wheat bran slag adds Broken kernel enzyme, Broken kernel enzyme add quality be wheat bran slag gross mass 0.03%-0.3%, react 0.5-5h after obtain through Cross the wheat bran slurry of pretreatment;
(2) it is 4%- to add distilled water in the wheat bran slurry by pretreatment obtained to step (1) and size mixing again to wine with dregs concentration 25%, and Ph to 6.0-10.0 is adjusted with the sodium hydroxide solution that mass concentration is 4%, it is 55-100 DEG C by temperature adjustment, base Alkali protease is added in wheat bran gross weight, the 1.0-3.0% that quality is wheat bran gross weight is added, is centrifuged after reacting 1-5h Separation, described centrifugal rotational speed is 2000-5000rpm, is freeze-dried after taking supernatant concentration, you can obtains the production of wheat bran albumen Product.
2. the method for two steps enzymolysis and extraction wheat bran albumen according to claim 1, it is characterised in that:Described in step (1) Size mixing after wine with dregs concentration be 15%;Described pH is 5.5;Described temperature is 50 DEG C;Described Broken kernel enzyme is promise The Viscozyme L of Wei Xin preparations Co., Ltd;The enzyme amount added is 0.2% based on wheat bran gross weight;Described reaction Time is 2.5h.
3. the method for two steps enzymolysis and extraction wheat bran albumen according to claim 1, it is characterised in that:Described in step (2) The wine with dregs concentration sized mixing again be 10%;Described pH is 8.0;Described temperature is 80 DEG C;Described alkali protease is promise The Alcalase 2.4L FG of Wei Xin preparations Co., Ltd;The enzyme amount added is the 2.0% of wheat bran gross weight;Reaction time is 2h;Described centrifugal rotational speed is 4000rpm.
4. the method for two steps enzymolysis and extraction wheat bran albumen according to claim 1, it is characterised in that:The step 1) obtains Slurry without other handle, be directly used in step 2).
5. the method for two steps enzymolysis and extraction wheat bran albumen according to claim 1, it is characterised in that:Need not in methods described Add the reactant such as alkali or acid to be reacted, the alkali includes inorganic base or organic base, and the acid includes inorganic acid or organic acid.
CN201710851711.3A 2017-09-19 2017-09-19 A kind of method of two steps enzymolysis and extraction wheat bran albumen Pending CN107446979A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710851711.3A CN107446979A (en) 2017-09-19 2017-09-19 A kind of method of two steps enzymolysis and extraction wheat bran albumen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710851711.3A CN107446979A (en) 2017-09-19 2017-09-19 A kind of method of two steps enzymolysis and extraction wheat bran albumen

Publications (1)

Publication Number Publication Date
CN107446979A true CN107446979A (en) 2017-12-08

Family

ID=60497785

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710851711.3A Pending CN107446979A (en) 2017-09-19 2017-09-19 A kind of method of two steps enzymolysis and extraction wheat bran albumen

Country Status (1)

Country Link
CN (1) CN107446979A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108866133A (en) * 2018-07-12 2018-11-23 天津科技大学 Pressure difference pretreatment collaboration high density fermentation wheat bran produces wheat bran oligopeptide method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102627694A (en) * 2012-03-29 2012-08-08 常熟市珍门麦芽糖厂 Method for extracting wheat bran protein
CN106858035A (en) * 2017-04-11 2017-06-20 中国科学院青岛生物能源与过程研究所 A kind of method of two steps enzymolysis and extraction rice bran protein

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102627694A (en) * 2012-03-29 2012-08-08 常熟市珍门麦芽糖厂 Method for extracting wheat bran protein
CN106858035A (en) * 2017-04-11 2017-06-20 中国科学院青岛生物能源与过程研究所 A kind of method of two steps enzymolysis and extraction rice bran protein

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
杜亚军: "小米糠深加工研究进展", 《粮食与饲料工业》 *
王乔等: "两步酶解提取米糠蛋白的工艺研究及优化", 《氨基酸和生物资源》 *
管骁: "复合多糖酶Viscozyme L在制备燕麦麸分离蛋白中的应用", 《农业工程学报》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108866133A (en) * 2018-07-12 2018-11-23 天津科技大学 Pressure difference pretreatment collaboration high density fermentation wheat bran produces wheat bran oligopeptide method
CN108866133B (en) * 2018-07-12 2022-03-04 天津科技大学 Method for producing wheat bran oligopeptide by virtue of synergistic high-density fermentation of wheat bran through differential pressure pretreatment

Similar Documents

Publication Publication Date Title
CN102907558B (en) Processing method of sea cucumber polypeptide
Sadh et al. Bio-enrichment of functional properties of peanut oil cakes by solid state fermentation using Aspergillus oryzae
US20090318670A1 (en) Separation of Proteins from Grasses Integrated with Ammonia Fiber Explosion (AFEX) Pretreatment and Cellulose Hydrolysis
CN103232522B (en) Method for coproducing and preparing malt syrup and proteins from broken rice
CN102115734B (en) Special compound enzyme for yeast hydrolysis and preparation method thereof
US20110201091A1 (en) Production of microbial growth stimulant with ammonia fiber explosion (AFEX) pretreatment and cellulose hydrolysis
CN102204620B (en) Method for preparing bitterless protein peptides
CN103704462B (en) Extraction and purification method for sesame proteins
CN104839457A (en) Method for preparing small peptide-enriched protein feed material based on steam explosion in combination with solid enzymatic hydrolysis
CN1230965A (en) Enzymatic degradation of carbohydrates in protein isolation methods
Bandara et al. Protein extraction from triticale distillers grains
SE461659B (en) PROCEDURES FOR PREPARING ENZYMET SPS-AS WITH THE ABILITY TO SUBSTITUTE HIGH-MOLECULE CARBON HYDROGEN
CN112592951B (en) Corn protein peptide and extraction method thereof
CN104928339B (en) A kind of preparation method with the oat protein peptide for inhibiting intestinal inflammatory activity
CN106173186A (en) The new method of polypeptide prepared by a kind of high-valued comprehensive utilization Fructus Tritici aestivi
CN107446979A (en) A kind of method of two steps enzymolysis and extraction wheat bran albumen
CN102771622A (en) Enzymolysis method for soyabean protein
Feng et al. Effect of solid-state fermentation on plant-sourced proteins: A review
CN110897059A (en) Method for preparing plant hydrolyzed protein beverage by using wheat germs
CN110713514A (en) Extraction method of wheat small molecule active peptide
CN102627694A (en) Method for extracting wheat bran protein
CN102277403B (en) Production technology of yellow wine lees proteins by enzymatic extraction
CN113151382B (en) Method for producing wheat oligopeptide by precipitation method
CN106858035A (en) A kind of method of two steps enzymolysis and extraction rice bran protein
CN103931872A (en) Distiller's grain cottonseed meal soluble protein powder and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20171208