CN101805077B - Treating method of paper-making water recycling use in the production process of reconstituted tobacco - Google Patents

Treating method of paper-making water recycling use in the production process of reconstituted tobacco Download PDF

Info

Publication number
CN101805077B
CN101805077B CN2010101627977A CN201010162797A CN101805077B CN 101805077 B CN101805077 B CN 101805077B CN 2010101627977 A CN2010101627977 A CN 2010101627977A CN 201010162797 A CN201010162797 A CN 201010162797A CN 101805077 B CN101805077 B CN 101805077B
Authority
CN
China
Prior art keywords
water
pulp
production process
grasped
ultra
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.)
Active
Application number
CN2010101627977A
Other languages
Chinese (zh)
Other versions
CN101805077A (en
Inventor
郑松明
潘雪松
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.)
Guangdong Jinke Reconstituted Tobacco Leaves Co Ltd
Original Assignee
Guangdong Jinke Reconstituted Tobacco Leaves 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 Guangdong Jinke Reconstituted Tobacco Leaves Co Ltd filed Critical Guangdong Jinke Reconstituted Tobacco Leaves Co Ltd
Priority to CN2010101627977A priority Critical patent/CN101805077B/en
Publication of CN101805077A publication Critical patent/CN101805077A/en
Application granted granted Critical
Publication of CN101805077B publication Critical patent/CN101805077B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)
  • Paper (AREA)

Abstract

The invention relates to a treating method of paper-making water recycling use in the production process of reconstituted tobacco, aiming at solving the problems that the massive discharge of treated water in the prior art causes pollution to the environment as well as low utilization ratio of water for production and large new-water consumption. The technical key points are characterized by carrying out fiber recovery on the paper-making water, then carrying out sedimentation, leading supernatant overflowing liquid after sedimentation into an ultrafiltration membrane separating system for separation, obtaining dislysate and concentrate, leading the dislysate into a reverse osmosis membrane system for separation again, obtaining purified water and concentrated water; the purified water is reused for water in the production process after treatment of removing off-odor, the recovered fiber is reused into the production process, the sediment is used as solid waste, the concentrate and the concentrated water are treated properly, the ultrafiltration membrane separating system adopts an ultrafiltration membrane with the bore diameter of 10-200nm, the pressure is 0.1-0.5MPa, the temperature of the feed liquid is 10-70 DEG C, the speed of the membrane surface is 2-8m/s, the pressure of the reverse osmosis membrane system is 1.0-10MPa, the temperature of the feed liquid is 20-45 DEG C, and the speed of the membrane surface is 2-7m/s.

Description

The treatment process that the water cycle of manufacturing paper with pulp in a kind of reconstituted tobacco production process is used
Technical field
The invention belongs to the processing method of cigarette making processes, particularly paper process production reconstituted tobacco process is handled so that the method that recycles the water of manufacturing paper with pulp.
Background technology
Present production of cigarettes has been different from traditional production method, one of its characteristics are the pipe tobaccos that adds a certain amount of reconstituted tobacco in pipe tobacco, with service performance, the processing characteristics of improving cigarette and cut the waste and reduce pollution, add-on generally can reach 20~30%.Reconstituted tobacco is also referred to as tobacco sheet, recombination tobacco leaf or homogeneous tobacco leaf etc., and papermaking-method reconstituted tobaccos is exactly to adopt papermaking process to make the reconstituted tobacco that obtains.The making method of papermaking-method reconstituted tobaccos is to be main raw material with tobacco materials such as offal, offal, tobacco leaf fragment, inferior tobaccos, pulverize defibrination and become tobacco slurry, with the chemical industry extraction and separation technology soluble chemical composition of tobacco slurry is separated adjustment, adopt the slag charge after system oar paper technology will be extracted to manufacture paper with pulp into substrate then, will separate the extraction component reduction of adjusting (as coating) then and to substrate, be processed to form the reconstituted tobacco product.
In the papermaking-method reconstituted tobaccos production process, there is the water of manufacturing paper with pulp in a large number (mthod of white water from paper making) to discharge by the wet end of paper machine, contain materials such as a certain amount of fiber fines, filler, tobacco extract in this part water.If this portion water is directly entered sewage works, not only increase the load of sewage works, the more important thing is the discharging large amount of sewage, cause the waste of water resources.Along with China to the fulfiling of international " Framework Convention on Tobacco Control ", tobacco industry is had higher requirement to the sewage disposal of papermaking-method reconstituted tobaccos production process.Water can be back in the papermaking-method reconstituted tobaccos production process if manufacture paper with pulp, and then can reclaim fiber fines material wherein, reduces the consumption of new water, the economical environment-protective cost, but also can alleviate the environmental pollution that causes because of discharge of wastewater.But contain the existence of a certain amount of tobacco extract in the water owing to manufacture paper with pulp, there are a lot of problems in direct reuse, particularly in that to recycle number of times more, envrionment temperature is than higher season, the water capacity of manufacturing paper with pulp is perishable smelly, have influence on the reconstituted tobacco product quality after the reuse, make quality product, or outward appearance is all stable inadequately no matter from endoplasm.
Chinese patent discloses a kind of wastewater from manufacture of tobacco slice by papermaking process treatment process No. 200410022326.0, the steps include: that waste water is after coarse filtration, enter the preliminary sedimentation tank precipitate and separate, the upper strata waste water of preliminary sedimentation tank is pumped into air flotation pool, and in the air flotation pool inlet channel with the coagulating agent thorough mixing, wherein most suspended solids will form floatation of foam in the air flotation pool liquid level with empty G﹠W, remove the suspended solid of liquid level by slag scraper in the mode of air supporting method, clear liquid enters equalizing tank then, cellulosic contained in the waste water is removed, send into the aeration tank then and handle, remove organic substance in most of water, can emit then by aerobic microbiological.The defective of this technological method is: added chemical substances such as coagulating agent in waste water, water after the processing has the residual of these chemical substances, so the water after handling can not be back to use in the papermaking-method reconstituted tobaccos production process, water after this processing of a large amount of dischargings still can cause certain pollution to environment, some place simply is exactly the discharging of forbidding this water, also cause the utilization ratio of production process water low on the other hand, the consumption of water is big.
Summary of the invention
For the water of manufacturing paper with pulp that overcomes existing similar technology existence can not be back to use in the papermaking-method reconstituted tobaccos production process, water after this processing of a large amount of dischargings can cause certain pollution to environment, cause the utilization ratio of production process water low simultaneously, the defective that the consumption of water is big, the objective of the invention is to disclose the treatment process that water cycle uses of manufacturing paper with pulp in a kind of improved reconstituted tobacco production process, can overcome the defective of prior art.
The technical solution adopted for the present invention to solve the technical problems is: the treatment process that the water cycle of manufacturing paper with pulp in a kind of reconstituted tobacco production process is used is characterized in that method steps is:
1., the water of manufacturing paper with pulp that the process of manufacturing paper with pulp in the reconstituted tobacco production is produced carries out recycled fiber earlier, imports settling tank or settling vessel then and carries out precipitation process, leads the supernatant overflowing liquid of getting after the precipitation process;
2., the supernatant overflowing liquid being imported the ultra-filtration membrane separation system separates, it is the ultra-filtration membrane of 10~200nm that the membrane element of ultra-filtration membrane separation system adopts the separation aperture, the working pressure of ultra-filtration membrane separation system is grasped at 0.1~0.5 MPa, feed temperature is grasped at 10~70 ℃, face speed is grasped at 2~8 m/s, obtains dialyzate and the dense water that contains solid insoluble, colloid, organic macromolecule material;
3., dialyzate imported reverse osmosis membrane system further separate, the working pressure of reverse osmosis membrane system is grasped at 1.0~10 MPa, feed temperature is grasped at 20~45 ℃, face speed is grasped at 2~7 m/s; Be purified water and condensed water;
4., will purify waste water eliminate the unusual smell handle after, reuse is a papermaking-method reconstituted tobaccos production process water;
5., the fiber of Hui Shouing is back to use in the papermaking-method reconstituted tobaccos production process, the throw out of precipitation process is disposed as solid refuse, and the condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that the ultra-filtration membrane separation system produces and reverse osmosis membrane system produce is dealt carefully with.
The recycled fiber of technique scheme can adopt filter method.
The condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that the ultra-filtration membrane separation system of technique scheme produces and reverse osmosis membrane system produce is dealt carefully with, and can adopt biochemical treatment, mix processing mode such as coal burning.
The processing that eliminates the unusual smell of technique scheme can adopt active-carbon bed, UV-device or ozone equipment etc. to remove peculiar smell.
Purifying waste water of technique scheme, the considerably less quite purified water of ionic impurity content that obtains by reverse osmosis membrane system exactly.
Beneficial effect of the present invention: the one, the water zero discharge or measure few innocuousness discharging of can accomplishing to manufacture paper with pulp has improved the degree of protection at environment and water source, also make simultaneously papermaking-method reconstituted tobaccos production become a kind of can generally accepted green production; The 2nd, by the processing of the inventive method, the water reuse amount of manufacturing paper with pulp reaches 70~90%, the utilization ratio height of production process water, and new water consumption reduces greatly; The 2nd, the dense water that need deal carefully with and the amount of condensed water are fewer, make it to become harmless emission water after the higher biochemical treatment of cost and solid refuse also can be born by producing even adopt, and quantity discharged is much less also, can digest for naturally; The 4th, ultra-filtration membrane separation and reverse osmosis membrane separation belong to the isolation technique of no phase transformation, not only its energy consumption is low, separating effect is good especially, the electric energy when only consuming the pumping feed liquid, and also operational management is simple, m of e is convenient, automated operation easily, it is few to drop into manpower, the operating environment health, the result favorable reproducibility, quality of reused water is stable.
Below in conjunction with embodiment the present invention is done to describe more specifically.
Embodiment
Embodiment one:The treatment process that the water cycle of manufacturing paper with pulp in this reconstituted tobacco production process is used is characterized in that method steps is:
1., the water of manufacturing paper with pulp that the process of manufacturing paper with pulp in the reconstituted tobacco production is produced carries out the filtered and recycled fiber earlier, imports settling tank or settling vessel then and carries out precipitation process, gets the supernatant overflowing liquid 54.0Kg after the precipitation process;
2., the supernatant overflowing liquid being imported the ultra-filtration membrane separation system separates, it is the ultra-filtration membrane of 10~200nm that the membrane element of ultra-filtration membrane separation system adopts the separation aperture, the working pressure of ultra-filtration membrane separation system is grasped at 0.3MPa, feed temperature is grasped at 23~35 ℃, face speed is grasped at 5 m/s, obtains dialyzate 51.2Kg and the dense water 2.8Kg that contains solid insoluble, colloid, organic macromolecule material;
3., dialyzate imported reverse osmosis membrane system further separate, the working pressure of reverse osmosis membrane system is grasped at 1.4MPa~2.2 MPa, feed temperature is grasped at 30~36 ℃, face speed is grasped at 4 m/s; Be purified water 46.2Kg and condensed water 5Kg;
4., will purify waste water by active-carbon bed eliminate the unusual smell handle after, reuse is a papermaking-method reconstituted tobaccos production process water, the water total yield of manufacturing paper with pulp is: 85.5%;
5., the fiber of Hui Shouing is back to use in the papermaking-method reconstituted tobaccos production process, the throw out of precipitation process is disposed as solid refuse, and the condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that the ultra-filtration membrane separation system produces and reverse osmosis membrane system produce is used to mix coal and burns.
Embodiment two:The treatment process that the water cycle of manufacturing paper with pulp in this reconstituted tobacco production process is used is characterized in that method steps is:
1., the water of manufacturing paper with pulp that the process of manufacturing paper with pulp in the reconstituted tobacco production is produced carries out the filtered and recycled fiber earlier, imports settling tank or settling vessel then and carries out precipitation process, gets the supernatant overflowing liquid 600Kg after the precipitation process;
2., the supernatant overflowing liquid being imported the ultra-filtration membrane separation system separates, it is the ultra-filtration membrane of 10~200nm that the membrane element of ultra-filtration membrane separation system adopts the separation aperture, the working pressure of ultra-filtration membrane separation system is grasped at 0.3MPa, feed temperature is grasped at 23~58 ℃, face speed is grasped at 4 m/s, obtains dialyzate 554.7Kg and the dense water 45.3Kg that contains solid insoluble, colloid, organic macromolecule material;
3., dialyzate imported reverse osmosis membrane system further separate, the working pressure of reverse osmosis membrane system is grasped at 1.2MPa~3.0 MPa, feed temperature is grasped at 32~38 ℃, face speed is grasped at 4 m/s; Be purified water 475.9Kg and condensed water 78.8Kg;
4., will purify waste water by internal diameter 10cm filling have an appointment the activated carbon adsorption bed of 3Kg gac eliminate the unusual smell handle after, reuse is a papermaking-method reconstituted tobaccos production process water, the water total yield of manufacturing paper with pulp is: 79.4%;
5., the fiber of Hui Shouing is back to use in the papermaking-method reconstituted tobaccos production process, the throw out of precipitation process is disposed as solid refuse, and the condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that the ultra-filtration membrane separation system produces and reverse osmosis membrane system produce is used to mix coal and burns.
Embodiment three:The treatment process that the water cycle of manufacturing paper with pulp in this reconstituted tobacco production process is used is characterized in that method steps is:
1., the water of manufacturing paper with pulp that the process of manufacturing paper with pulp in the reconstituted tobacco production is produced carries out the filtered and recycled fiber earlier, imports settling tank or settling vessel then and carries out precipitation process, gets the supernatant overflowing liquid 900Kg after the precipitation process;
2., the supernatant overflowing liquid being imported the ultra-filtration membrane separation system separates, it is the ultra-filtration membrane of 10~200nm that the membrane element of ultra-filtration membrane separation system adopts the separation aperture, the working pressure of ultra-filtration membrane separation system is grasped at 0.3MPa, feed temperature is grasped at 28~60 ℃, face speed is grasped at 5 m/s, obtains dialyzate 844Kg and the dense water 56Kg that contains solid insoluble, colloid, organic macromolecule material;
3., dialyzate imported reverse osmosis membrane system further separate, the working pressure of reverse osmosis membrane system is grasped at 1.6MPa~3.3 MPa, feed temperature is grasped at 30~40 ℃, face speed is grasped at 6 m/s; Be purified water 671.0Kg and condensed water 173.0Kg;
4., will purify waste water by in the recycle system that has ozonizer, after the circulation through after a while eliminated the unusual smell and handles, reuse was a papermaking-method reconstituted tobaccos production process water, the water total yield of manufacturing paper with pulp is: 74.6%;
5., the fiber of Hui Shouing is back to use in the papermaking-method reconstituted tobaccos production process, the throw out of precipitation process is disposed as solid refuse, and the condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that the ultra-filtration membrane separation system produces and reverse osmosis membrane system produce is used to mix coal and burns.
Below be that water sample with three embodiment carries out water quality analysis, and the table that detected result is gathered:
In the table: COD is a chemical oxygen demand (COD); BOD is a biochemical oxygen demand (BOD); SS is a solid suspension.

Claims (5)

1. the treatment process that the water cycle of manufacturing paper with pulp in the reconstituted tobacco production process is used is characterized in that method steps is:
1., the water of manufacturing paper with pulp that the process of manufacturing paper with pulp in the reconstituted tobacco production is produced carries out recycled fiber earlier, imports settling tank or settling vessel then and carries out precipitation process, leads the supernatant overflowing liquid of getting after the precipitation process;
2., the supernatant overflowing liquid being imported the ultra-filtration membrane separation system separates, it is the ultra-filtration membrane of 10~200nm that the membrane element of ultra-filtration membrane separation system adopts the separation aperture, the working pressure of ultra-filtration membrane separation system is grasped at 0.1~0.5 MPa, feed temperature is grasped at 10~70 ℃, face speed is grasped at 2~8 m/s, obtains dialyzate and the dense water that contains solid insoluble, colloid, organic macromolecule material;
3., dialyzate imported reverse osmosis membrane system further separate, the working pressure of reverse osmosis membrane system is grasped at 1.0~10 MPa, feed temperature is grasped at 20~45 ℃, face speed is grasped at 2~7 m/s; Be purified water and condensed water;
4., will purify waste water eliminate the unusual smell handle after, reuse is a papermaking-method reconstituted tobaccos production process water;
5., the fiber of Hui Shouing is back to use in the papermaking-method reconstituted tobaccos production process, the throw out of precipitation process is disposed as solid refuse, and the condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that the ultra-filtration membrane separation system produces and reverse osmosis membrane system produce is dealt carefully with.
2. the treatment process of using by the water cycle of manufacturing paper with pulp in the described reconstituted tobacco production process of claim 1, it is characterized in that the condensed water that dense water that contains solid insoluble, colloid, organic macromolecule material that described ultra-filtration membrane separation system produces and reverse osmosis membrane system produce deals carefully with, is to adopt biochemical treatment or mix the processing mode that coal burns.
3. the treatment process of using by the water cycle of manufacturing paper with pulp in claim 1 or the 2 described reconstituted tobacco production processes is characterized in that described recycled fiber adopts filter method.
4. the treatment process of using by the water cycle of manufacturing paper with pulp in claim 1 or the 2 described reconstituted tobacco production processes is characterized in that the described processing that eliminates the unusual smell, and adopts active-carbon bed, UV-device or ozone equipment to remove peculiar smell.
5. the treatment process of using by the water cycle of manufacturing paper with pulp in the described reconstituted tobacco production process of claim 4, it is characterized in that the active-carbon bed peculiar smell of removing of described employing, is to purify waste water by the internal diameter 10cm filling activated carbon adsorption bed of the 3Kg gac processing that eliminates the unusual smell of having an appointment.
CN2010101627977A 2010-04-29 2010-04-29 Treating method of paper-making water recycling use in the production process of reconstituted tobacco Active CN101805077B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010101627977A CN101805077B (en) 2010-04-29 2010-04-29 Treating method of paper-making water recycling use in the production process of reconstituted tobacco

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010101627977A CN101805077B (en) 2010-04-29 2010-04-29 Treating method of paper-making water recycling use in the production process of reconstituted tobacco

Publications (2)

Publication Number Publication Date
CN101805077A CN101805077A (en) 2010-08-18
CN101805077B true CN101805077B (en) 2011-08-03

Family

ID=42607060

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010101627977A Active CN101805077B (en) 2010-04-29 2010-04-29 Treating method of paper-making water recycling use in the production process of reconstituted tobacco

Country Status (1)

Country Link
CN (1) CN101805077B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102531285B (en) * 2011-12-30 2013-07-17 福建金闽再造烟叶发展有限公司 Process for treating high-concentration organic wastewater of paper-making reconstituted tobacco
CN102599638A (en) * 2012-01-11 2012-07-25 福建金闽再造烟叶发展有限公司 Low-retention monolayer net papermaking process of reconstituted tobaccos by papermaking method and equipment thereof
CN103892457B (en) * 2013-05-29 2016-08-10 广东金科再造烟叶有限公司 A kind of paper process tobacco extraction liquid process for refining
CN103549641B (en) * 2013-11-14 2016-01-06 红塔烟草(集团)有限责任公司 The purifying treatment method that stalk water circulation uses is washed in a kind of papermaking-method reconstituted tobaccos production process
CN103663628A (en) * 2013-12-13 2014-03-26 北京清大膜科膜技术有限公司 Ultrafiltration device for processing papermaking wastewater and application method thereof
CN103829365A (en) * 2014-03-18 2014-06-04 广东省金叶科技开发有限公司 Corrosion-prevention method for paper-making process reconstituted tobacco production white water system
CN105198116B (en) * 2015-08-31 2017-07-18 南京林业大学 The method for producing waste water is reduced in a kind of clean paper making
CN107487875A (en) * 2017-08-24 2017-12-19 上海烟草集团有限责任公司 A kind of papermaking-method reconstituted tobaccos are manufactured paper with pulp white water recycling handling process
CN110066037A (en) * 2019-05-20 2019-07-30 上海烟草集团有限责任公司 A kind of reconstituted tobacco plain boiled water processing method and system

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4242517C1 (en) * 1992-12-16 1994-01-27 Daimler Benz Ag Lacquering plant operating process - uses bio-reactor and membrane separator to regenerate circulated water
FR2702469A1 (en) * 1993-03-12 1994-09-16 Egretier Jean Michel Device for purifying aqueous effluents
CN1289415C (en) * 2004-04-15 2006-12-13 云南瑞升科技有限公司 Processing technology for tobacco thin sheet waste water by paper-making method
CN100526240C (en) * 2007-01-12 2009-08-12 华南理工大学 Method for anerobic aerobic granular sludge treating high concentration waste water from paper-making method tobacco slice production

Also Published As

Publication number Publication date
CN101805077A (en) 2010-08-18

Similar Documents

Publication Publication Date Title
CN101805077B (en) Treating method of paper-making water recycling use in the production process of reconstituted tobacco
CN105714590B (en) Separating lignin and hemicellulose and the method for reclaiming alkali lye from black liquid
CN101591085A (en) A kind of wastewater treatment and reuse technology for paper mill
CN103349867B (en) Paper-making process reconstituted tobacco papermaking white water reuse treatment method
CN101731736B (en) Solid-liquid enrichment separation method for tobacco sheet wastewater in paper-making method
CN112808738A (en) Method for preparing carbon source by utilizing kitchen waste
CN105776726A (en) Treatment process of printing and dyeing wastewater in textile industry
CN106116023A (en) A kind of method of work of Waste Water Treatment
CN102515395A (en) Method and device for using small-aperture spiral wound ultrafiltration membranes to treat papermaking wastewater
CN102633405B (en) Treatment method of papermaking black liquor
CN102531285B (en) Process for treating high-concentration organic wastewater of paper-making reconstituted tobacco
CN104310720A (en) Method for treating paper-making wastewater
CN103922505A (en) Method for deep treatment on tea bag filter paper making bleach by using nanofiltration membrane
CN210103778U (en) Sea sand desalination device
CN112251331A (en) Dry anaerobic fermentation system for dry and wet sorting pretreatment of kitchen waste and treatment method thereof
CN103726386A (en) Method and system for realizing zero emission of papermaking pulp residue and sludge
WO2009021552A1 (en) Improved separation/purification method / installation for aqueous liquid dispersions of organic material, and use of such method / installation in an integrated treatment of manure and/or organic disgestates
KR101412521B1 (en) Salt and solid content processing system/method of food waste
CN107487875A (en) A kind of papermaking-method reconstituted tobaccos are manufactured paper with pulp white water recycling handling process
CN209210582U (en) A kind of reducing rules wastewater membrane separation coupling evaporating
US20150041405A1 (en) Method and Installation for Processing Raw Liquid Manure and/or Fermentation Residues from Biogas Production
CN205035216U (en) Paper mill plain boiled water multilevel processing recycling system
CN105254100B (en) A kind of saline sewage processing system and method
CN106746225A (en) Device and method for recovering potato starch production wastewater
CN104724841A (en) Method for recovery of oligomer and monomer from polyamide water extraction solution distillation liquid and recycling of process water

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: GUANGDONG JINKE RECONSTITUTED TOBACCO CO., LTD.

Free format text: FORMER OWNER: GUANGDONG GOLD LEAF TOBACCO SHEET TECHNOLOGY DEVELOPMENT CO., LTD.

Effective date: 20101220

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 515041 31/F, YOUYI INTERNATIONAL BUILDING, NO. 86, JINSHA ROAD, SHANTOU CITY, GUANGDONG PROVINCE TO: 515100 INSIDE DEMING INDUSTRIAL ZONE, JINKE ROAD, CHAOYANG DISTRICT, SHANTOU CITY, GUANGDONG PROVINCE

TA01 Transfer of patent application right

Effective date of registration: 20101220

Address after: 515100 Guangdong Province, Shantou city Chaoyang District Jinke road Deming Industrial Zone

Applicant after: Guangdong Jinke Reconstituted Tobacco Co., Ltd.

Address before: 31, friendship International Building, No. 86 Jin Sha Road, 515041, Guangdong, Shantou

Applicant before: Guangdong Jinye Tobacco Sheet Technology Development Co., Ltd.

C14 Grant of patent or utility model
GR01 Patent grant