CN106546067A - Bacterial cellulose gel film replaces low temperature integrated dry drying system - Google Patents

Bacterial cellulose gel film replaces low temperature integrated dry drying system Download PDF

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Publication number
CN106546067A
CN106546067A CN201510596535.4A CN201510596535A CN106546067A CN 106546067 A CN106546067 A CN 106546067A CN 201510596535 A CN201510596535 A CN 201510596535A CN 106546067 A CN106546067 A CN 106546067A
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China
Prior art keywords
displacer
drying chamber
hold
tank
entrance
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Granted
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CN201510596535.4A
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Chinese (zh)
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CN106546067B (en
Inventor
钟春燕
钟宇光
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Hainan Yeguo Foods Co Ltd
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Hainan Yeguo Foods Co Ltd
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  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

Present invention offer is a kind of can to enter the system that line replacement, low temperature integral type are dried to bacterial cellulose gel film, and which mainly includes:Drying chamber(1)With displacer hold-up tank(2), the drying chamber(1)Top is provided with valvular gas outlet(3), drying chamber(1)Bottom is provided with valvular outlet(4)With displacer entrance(5), and electric heater unit(6), the central shaft rod that can be removed is set at drying chamber axis(7);The displacer hold-up tank(2)Top arranges displacer and reclaims entrance(8), displacer hold-up tank(2)Bottom arranges displacer outlet(9), the drying chamber(1)The valvular gas outlet of band on top(3)With displacer hold-up tank(2)The displacer on top reclaims entrance(8)Connected by conduit, the drying chamber(1)The displacer entrance of bottom(5)By with displacer hold-up tank(2)The displacer outlet of bottom(9)Connected by conduit.

Description

Bacterial cellulose gel film replaces low temperature integrated dry drying system
Technical field
The present invention relates to a kind of material drying system, replaces low temperature integrated dry drying system in particular to a kind of bacterial cellulose gel film.
Background technology
Bacterial cellulose is to be synthesized the biomaterial for obtaining by some microbial metabolisms, which has similar basic structure with native cellulose, but due to wherein not containing the association product such as lignin, hemicellulose, simultaneously with up to more than 95% degree of crystallinity and the up to high polymerization degree of 2000-8000, and there is the property of many uniquenesses, for example, which has outstanding mechanical performance, well higher biocompatibility, biodegradability etc..Which has widely application prospect in multiple technical fields.Bacterial cellulose obtains having very high-moisture bacterial cellulose gel film mainly by liquid culture medium static fermentation culture at present.But, in increasing application, need using substantially free of water drying bacteria cellulose membrane.Conventional drying meanss mainly have the modes such as hot-air drying, lyophilization, but high temperature and freezing inevitably produce impact to the space net structure of Bacterial cellulose, so as to affect many Wuli-Shili-Renli system approach of bacteria cellulose film, such as porosity, mechanical performance, electric conductivity etc..Although the Supercritical Drying Technology of rising in recent years can keep the space net structure of Bacterial cellulose to greatest extent, which is with high costs, and the requirement to equipment is very high, also rests on laboratory stage at present and industrially can not apply on a large scale.
The content of the invention
Present invention offer is a kind of can to enter the system that line replacement, low temperature integral type are dried to bacterial cellulose gel film, and which mainly includes:Drying chamber and displacer hold-up tank, the drying chamber top are provided with valvular gas outlet, and drying chamber bottom is provided with valvular outlet and displacer entrance, and electric heater unit, and the central shaft rod that can be removed is arranged at drying chamber axis;The displacer hold-up tank top arranges displacer and reclaims entrance, displacer hold-up tank bottom arranges displacer outlet, the valvular gas outlet of band on the drying chamber top is reclaimed entrance with the displacer on displacer hold-up tank top and is connected by conduit, and the displacer entrance of the drying chamber bottom is connected by conduit by the displacer outlet with displacer hold-up tank bottom.
In said system, on the side wall of drying chamber 1, transparent windows are also set up, to the position for observing liquid level.It is preferred which extends to is dried pot bottom.
In said system, whether the electric heater unit passes through temperature sensor and temperature regulating device is controlled, started by the temperature control heater in temperature sensor measurement drying chamber.
In said system, the valvular gas outlet of band on drying chamber top is reclaimed entrance with the displacer on displacer hold-up tank top and is connected by condenser and conduit.
In said system, the displacer entrance of drying chamber bottom is connected by pump and conduit by the displacer outlet with displacer hold-up tank bottom.Described pump can be bidirectional rotation.
Displacement low temperature integrated dry drying system provided by the present invention, can first pass through displacement drying technology and the moisture in bacterial cellulose gel film is cemented out with displacer, then displacer be removed from bacteria cellulose film by cold drying technology.Displacement drying is carried out completely at normal temperatures, and cold drying also only need to be carried out at 50-60 DEG C according to the species of displacer, therefore, it is possible to avoid the destruction of high temperature or freezing to bacteria cellulose film space net structure, improves the properties of drying bacteria cellulose membrane.In addition, displacement low temperature drying system provided by the present invention carries out can also the displacement drying and cold drying integral type in the same tank body, multiple equipment is not needed, Bacterial cellulose material is shifted repeatedly, displacer recycling can also be reclaimed, it is with low cost, simple to operate, have a good application prospect.
Description of the drawings
The following drawings is only intended to do schematic illustration and explanation with to the present invention, not delimit the scope of the invention.Wherein:
Fig. 1 is the structural representation of the specific embodiment of the invention.
In figure:
1- drying chambers;2- displacer hold-up tanks;3- is with valvular gas outlet;4- is with valvular outlet;5- displacer entrances;6- electric heater units;7- central shaft rods;8- displacers reclaim entrance;9- displacers are exported;10- transparent windows;11- temperature sensors;12- temperature regulating devices;13- condensers;14- pumps.
Specific embodiment
Below in conjunction with the accompanying drawings the present invention is further elaborated.In following specific descriptions, only the present invention is described by way of explanation, and restriction effect is not played to which.Those of ordinary skill in the art can be modified to following concrete modes with various different modes, and which also should be within the scope of protection of the invention without departing from the spirit and scope of the invention.
As shown in Figure 1, in the bacterial cellulose gel film displacement low temperature integrated dry drying system that the present invention is provided, including drying chamber 1 and displacer hold-up tank 2,1 top of the drying chamber is provided with valvular gas outlet 3,1 bottom of drying chamber is provided with valvular outlet 4 and displacer entrance 5, and electric heater unit 6, the electric heater unit 6 passes through temperature sensor 11 and temperature regulating device 12 is controlled, and whether the temperature control heater 6 measured by temperature sensor 11 in drying chamber 1 starts.The central shaft rod 7 that can be removed is set at the drying chamber axis, its can remove after by aqueous bacterial cellulose gel film roll thereon after, then install back in drying chamber;2 top of displacer hold-up tank arranges displacer and reclaims entrance 8,2 bottom of displacer hold-up tank arranges displacer outlet 9, the valvular gas outlet 3 of band on 1 top of drying chamber is reclaimed entrance 8 with the displacer on 2 top of displacer hold-up tank and is connected by condenser 13, and the displacer entrance 5 of 1 bottom of drying chamber is connected by pump 14 by the displacer outlet 9 with 2 bottom of displacer hold-up tank.It is additionally provided with the side wall of the drying chamber 1 and extends to the transparent windows 10 for being dried pot bottom, to the position for observing liquid level.
Displacement low temperature integrated dry drying system working method of the present invention is as follows:
First, remove the central shaft rod 7 in drying chamber 1, by aqueous bacterial cellulose gel film roll in the central shaft rod 7, then installed back in drying chamber 1, the outlet 4 of the gas outlet 3, bottom on closing drying chamber top, displacer entrance 5 is opened, then the displacer in displacer hold-up tank 2 is pumped in drying chamber 1 by pump 14, when displacer liquid level is higher than bacterial cellulose gel film roll into drying chamber(Liquid level is observed by transparent windows), stopping pumping into displacer and close displacer entrance 5, standing carries out Solvent exchange drying.Displacer can enter bacterial cellulose gel film in moisture therein be cemented out, and due to displacer it is lighter than water, therefore, the liquid in drying chamber occurs layering, and lower floor is water, and upper strata is displacer.After displacement drying is finished, the outlet 3 for opening 1 bottom of drying chamber releases waste water, after waste water is discharged(Contain displacer or level change is observed by transparent windows when in the liquid that observable is released), close outlet 3, open displacer entrance 5, remaining displacer in drying chamber is pumped in displacer hold-up tank 2, after the completion of close displacer entrance 5.The gas outlet 3 on drying chamber top is opened again, start electric heater unit, and the temperature controlled by temperature sensor and temperature regulating device in drying chamber is slightly above the boiling point of displacer, make displacer become gaseous state and steam from gas outlet 3, and after condenser 13 is condensed, be back in displacer hold-up tank 2.

Claims (8)

1. a kind of bacterial cellulose gel film replaces low temperature integrated dry drying system, it is characterised in that mainly include:Drying chamber(1)With displacer hold-up tank(2), the drying chamber(1)Top is provided with valvular gas outlet(3), drying chamber(1)Bottom is provided with valvular outlet(4)With displacer entrance(5), and electric heater unit(6), the central shaft rod that can be removed is set at drying chamber axis(7);The displacer hold-up tank(2)Top arranges displacer and reclaims entrance(8), displacer hold-up tank(2)Bottom arranges displacer outlet(9), the drying chamber(1)The valvular gas outlet of band on top(3)With displacer hold-up tank(2)The displacer on top reclaims entrance(8)Connected by conduit, the drying chamber(1)The displacer entrance of bottom(5)By with displacer hold-up tank(2)The displacer outlet of bottom(9)Connected by conduit.
2. system according to claim 1, it is characterised in that:Drying chamber(1)Side wall on be additionally provided with transparent windows(10).
3. system according to claim 3, it is characterised in that:The transparent windows(10)Extend to and be dried pot bottom.
4. the system according to one of claim 1-3, it is characterised in that:The electric heater unit(6)Controlled by temperature sensor 11 and temperature regulating device 12.
5. the system according to one of claim 1-3, it is characterised in that:Drying chamber(1)The valvular gas outlet of band on top(3)Entrance is reclaimed with the displacer on 2 top of displacer hold-up tank(8)By condenser(13)Connect with conduit.
6. system according to claim 5, it is characterised in that:Drying chamber(1)The displacer entrance of bottom(5)By with displacer hold-up tank(2)The displacer outlet of bottom(9)By pump(14)Connect with conduit.
7. system according to claim 6, it is characterised in that:Described pump(14)It can be bidirectional rotation.
8. a kind of bacterial cellulose gel film replaces low temperature drying method, it is characterised in that:Usage right requires that the system described in any one of 1-7 enters line replacement cold drying to bacterial cellulose gel film.
CN201510596535.4A 2015-09-18 2015-09-18 Low-temperature integrated drying method for replacing bacterial cellulose gel film Active CN106546067B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107930543A (en) * 2017-12-28 2018-04-20 乐山职业技术学院 A kind of solvent displacement for being used to prepare aeroge and the device and method of constant pressure and dry

Citations (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB797605A (en) * 1955-07-25 1958-07-02 Patenthandels A G Apparatus for drying fibres
US3313092A (en) * 1963-05-17 1967-04-11 Dryvent Ltd Apparatus for fractionating gaseous mixtures
US3386181A (en) * 1966-11-15 1968-06-04 Du Pont Method of removing water and apparatus therefor
GB1201354A (en) * 1967-11-20 1970-08-05 Blaw Knox Co Removing solvent from free flowing material
US3559297A (en) * 1969-03-10 1971-02-02 Allied Chem Process and apparatus for removing water from solid surfaces
US3589023A (en) * 1969-06-10 1971-06-29 Allied Chem Process and apparatus for removing water from solid surfaces at low temperatures
US3653983A (en) * 1968-11-22 1972-04-04 Henkel & Cie Gmbh Compositions for displacing water adhering to metal surfaces and process
US3802090A (en) * 1971-07-22 1974-04-09 Jeumont Schneider Process and installation for drying fibrous cellulose materials
GB2038653A (en) * 1978-12-27 1980-07-30 Kloeckner Humboldt Deutz Ag Dressing Slurries
EP0194589A2 (en) * 1985-03-11 1986-09-17 AlliedSignal Inc. Apparatus and method for cleaning and drying surfaces of non-absorbent articles
US5458786A (en) * 1994-04-18 1995-10-17 The Center For Innovative Technology Method for dewatering fine coal
CN1121953A (en) * 1994-10-28 1996-05-08 奥林帕斯光学工业株式会社 Composition and method for washing and drying
CN1167779A (en) * 1996-04-11 1997-12-17 三井石油化学工业株式会社 Method of drying solid polymer and drying apparatus
JP2000070605A (en) * 1998-09-04 2000-03-07 Du Pont Mitsui Fluorochem Co Ltd Method and apparatus for draining/washing
CN1303881A (en) * 2000-01-07 2001-07-18 四川大学 Divided-flow solvent-removing and product-drying method for producing polyvinyl alcohol pellet
JP2004249250A (en) * 2003-02-21 2004-09-09 Denso Corp Draining and drying device
CN1658937A (en) * 2002-06-03 2005-08-24 财团法人电力中央研究所 Method for removing water contained in solid using liquid material
US20070025896A1 (en) * 2005-07-13 2007-02-01 Bitmin Resources Inc. Oil sand processing apparatus and control system
US20070295365A1 (en) * 2006-06-27 2007-12-27 Katsuhiko Miya Substrate processing method and substrate processing apparatus
CN101097837A (en) * 2006-06-27 2008-01-02 大日本网目版制造株式会社 Substrate processing method and substrate processing apparatus
CN101121666A (en) * 2006-08-11 2008-02-13 小仓合成工业株式会社 Process for producing amino compound
CN101168467A (en) * 2007-09-28 2008-04-30 天津大学 Sludge replacing and dewatering method and device
CN101398254A (en) * 2007-09-30 2009-04-01 浙江医药股份有限公司新昌制药厂 Peptide-containing antibiotic finished product drying method
CN101433562A (en) * 2008-12-17 2009-05-20 中国林业科学研究院林产化学工业研究所 Method for preparing ginkgo leaf extract powder using supercritical liquid desiccation and device thereof
US20090255876A1 (en) * 2008-04-11 2009-10-15 Dunbar James M Feedback control scheme for optimizing dewatering processes
CN101603772A (en) * 2009-06-11 2009-12-16 山东省科学院生物研究所 A kind of product drying and solvent recovery process and equipment
CN101666575A (en) * 2008-09-03 2010-03-10 淄博矿业集团有限责任公司 Drying process and drying system for material containing low-boiling point, inflammable and explosive organic solvent
CN101780390A (en) * 2009-01-16 2010-07-21 中国科学院过程工程研究所 Substitution and dehydration method for water contained solid materials and device
CN102040512A (en) * 2009-10-13 2011-05-04 中国石油化工股份有限公司 Crude terephthalic acid mother solution replacing method
CN102108001A (en) * 2009-12-24 2011-06-29 大连理工大学 Film pressure thermal dehydration method and equipment for high-moisture sludge
CN102141338A (en) * 2010-02-03 2011-08-03 株式会社川田 Drying device and replacement method of non-active gas
JP2011255353A (en) * 2010-06-11 2011-12-22 Asahi Glass Co Ltd Draining/drying method and draining/drying system
US20120047764A1 (en) * 2010-08-24 2012-03-01 David Campion System and method for drying substrates
US20120245399A1 (en) * 2011-03-22 2012-09-27 Marathon Gtf Technology, Ltd. Processes and systems for drying liquid bromine
CN103272539A (en) * 2013-05-07 2013-09-04 李光武 Method and device for preparing aerogel by drying under reduced pressure
WO2013183007A1 (en) * 2012-06-07 2013-12-12 Kemira Oyj High solids content microfibrillated cellulose and manufacturing thereof
CN104019639A (en) * 2014-06-07 2014-09-03 张家港市进润彩印包装有限公司 Solvent recoverable vacuum drying process
CN104064445A (en) * 2013-03-18 2014-09-24 芝浦机械电子装置股份有限公司 Substrate Processing Device And Substrate Processing Method
CN204017442U (en) * 2014-08-26 2014-12-17 浙江圣达生物药业股份有限公司 A kind of solvent separation unit
CN104334517A (en) * 2012-05-11 2015-02-04 莱姆泰克株式会社 Solvent-substitution solvent used in aerogel production, and hydrophobised aerogel production method using same
CN204424225U (en) * 2015-01-16 2015-06-24 弘塑科技股份有限公司 Integrated moisture removal and drying process equipment
CN205102512U (en) * 2015-09-18 2016-03-23 海南椰国食品有限公司 Bacteria cellulose gel mould replacement low temperature integral type drying system

Patent Citations (42)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB797605A (en) * 1955-07-25 1958-07-02 Patenthandels A G Apparatus for drying fibres
US3313092A (en) * 1963-05-17 1967-04-11 Dryvent Ltd Apparatus for fractionating gaseous mixtures
US3386181A (en) * 1966-11-15 1968-06-04 Du Pont Method of removing water and apparatus therefor
GB1201354A (en) * 1967-11-20 1970-08-05 Blaw Knox Co Removing solvent from free flowing material
US3653983A (en) * 1968-11-22 1972-04-04 Henkel & Cie Gmbh Compositions for displacing water adhering to metal surfaces and process
US3559297A (en) * 1969-03-10 1971-02-02 Allied Chem Process and apparatus for removing water from solid surfaces
US3589023A (en) * 1969-06-10 1971-06-29 Allied Chem Process and apparatus for removing water from solid surfaces at low temperatures
US3802090A (en) * 1971-07-22 1974-04-09 Jeumont Schneider Process and installation for drying fibrous cellulose materials
GB2038653A (en) * 1978-12-27 1980-07-30 Kloeckner Humboldt Deutz Ag Dressing Slurries
EP0194589A2 (en) * 1985-03-11 1986-09-17 AlliedSignal Inc. Apparatus and method for cleaning and drying surfaces of non-absorbent articles
US5458786A (en) * 1994-04-18 1995-10-17 The Center For Innovative Technology Method for dewatering fine coal
CN1121953A (en) * 1994-10-28 1996-05-08 奥林帕斯光学工业株式会社 Composition and method for washing and drying
CN1167779A (en) * 1996-04-11 1997-12-17 三井石油化学工业株式会社 Method of drying solid polymer and drying apparatus
JP2000070605A (en) * 1998-09-04 2000-03-07 Du Pont Mitsui Fluorochem Co Ltd Method and apparatus for draining/washing
CN1303881A (en) * 2000-01-07 2001-07-18 四川大学 Divided-flow solvent-removing and product-drying method for producing polyvinyl alcohol pellet
CN1658937A (en) * 2002-06-03 2005-08-24 财团法人电力中央研究所 Method for removing water contained in solid using liquid material
JP2004249250A (en) * 2003-02-21 2004-09-09 Denso Corp Draining and drying device
US20070025896A1 (en) * 2005-07-13 2007-02-01 Bitmin Resources Inc. Oil sand processing apparatus and control system
US20070295365A1 (en) * 2006-06-27 2007-12-27 Katsuhiko Miya Substrate processing method and substrate processing apparatus
CN101097837A (en) * 2006-06-27 2008-01-02 大日本网目版制造株式会社 Substrate processing method and substrate processing apparatus
CN101121666A (en) * 2006-08-11 2008-02-13 小仓合成工业株式会社 Process for producing amino compound
CN101168467A (en) * 2007-09-28 2008-04-30 天津大学 Sludge replacing and dewatering method and device
CN101398254A (en) * 2007-09-30 2009-04-01 浙江医药股份有限公司新昌制药厂 Peptide-containing antibiotic finished product drying method
US20090255876A1 (en) * 2008-04-11 2009-10-15 Dunbar James M Feedback control scheme for optimizing dewatering processes
CN101666575A (en) * 2008-09-03 2010-03-10 淄博矿业集团有限责任公司 Drying process and drying system for material containing low-boiling point, inflammable and explosive organic solvent
CN101433562A (en) * 2008-12-17 2009-05-20 中国林业科学研究院林产化学工业研究所 Method for preparing ginkgo leaf extract powder using supercritical liquid desiccation and device thereof
CN101780390A (en) * 2009-01-16 2010-07-21 中国科学院过程工程研究所 Substitution and dehydration method for water contained solid materials and device
CN101603772A (en) * 2009-06-11 2009-12-16 山东省科学院生物研究所 A kind of product drying and solvent recovery process and equipment
CN102040512A (en) * 2009-10-13 2011-05-04 中国石油化工股份有限公司 Crude terephthalic acid mother solution replacing method
CN102108001A (en) * 2009-12-24 2011-06-29 大连理工大学 Film pressure thermal dehydration method and equipment for high-moisture sludge
CN102141338A (en) * 2010-02-03 2011-08-03 株式会社川田 Drying device and replacement method of non-active gas
JP2011255353A (en) * 2010-06-11 2011-12-22 Asahi Glass Co Ltd Draining/drying method and draining/drying system
US20120047764A1 (en) * 2010-08-24 2012-03-01 David Campion System and method for drying substrates
US20120245399A1 (en) * 2011-03-22 2012-09-27 Marathon Gtf Technology, Ltd. Processes and systems for drying liquid bromine
CN104334517A (en) * 2012-05-11 2015-02-04 莱姆泰克株式会社 Solvent-substitution solvent used in aerogel production, and hydrophobised aerogel production method using same
WO2013183007A1 (en) * 2012-06-07 2013-12-12 Kemira Oyj High solids content microfibrillated cellulose and manufacturing thereof
CN104064445A (en) * 2013-03-18 2014-09-24 芝浦机械电子装置股份有限公司 Substrate Processing Device And Substrate Processing Method
CN103272539A (en) * 2013-05-07 2013-09-04 李光武 Method and device for preparing aerogel by drying under reduced pressure
CN104019639A (en) * 2014-06-07 2014-09-03 张家港市进润彩印包装有限公司 Solvent recoverable vacuum drying process
CN204017442U (en) * 2014-08-26 2014-12-17 浙江圣达生物药业股份有限公司 A kind of solvent separation unit
CN204424225U (en) * 2015-01-16 2015-06-24 弘塑科技股份有限公司 Integrated moisture removal and drying process equipment
CN205102512U (en) * 2015-09-18 2016-03-23 海南椰国食品有限公司 Bacteria cellulose gel mould replacement low temperature integral type drying system

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
潘永康: "《现代干燥技术》", 30 September 1998 *
王连勇等: "置换干燥原理及其在木材干燥中的应用", 《节能》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107930543A (en) * 2017-12-28 2018-04-20 乐山职业技术学院 A kind of solvent displacement for being used to prepare aeroge and the device and method of constant pressure and dry
CN107930543B (en) * 2017-12-28 2023-08-11 乐山职业技术学院 Device and method for solvent replacement and normal-pressure drying for preparing aerogel

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