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`
`Espacenet - Bibliographic data
`
`Page 1 of 2
`
`
`
`Eaeacenet
`
`htiesareiiiiiisiiiiiiiitiéiéiEtta3iiEtta???Iiiiitati3-525tiiii-3t}tiiii-It?iiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiiii
`
`aereoo eoe ececraonrawaia area AeeAaArua Foe eaacreoctAtvaia
`
`|nventor(s):
`
`MASAMOTO MANABU; IZUMI NORIAKI; KONISHI SATOSHI;
`IKEDA MICHIHARU j; (MASAMOTO MANABU,
`; IZUMI NORIAKI, ;
`KONISHI SATOSHI, ; IKEDA MICHIHARU, 1512K e, ; rue eat;
`4% Hit
`,
`; ittEH are
`
`Applicant(s):
`
`KAWASAKI HEAVY IND LTD : (KAWASAKI HEAVY IND LTD,
`mealeeitee)
`
`; )II
`
`C|assificatiom - international: earner/44; Baffler/’46; career/area; 6135(1/92
`- cooperative: Y02A20i134
`
`Application
`number:
`
`JP20110048456 20110307
`
`Giohai Dossier
`
`Priority number JP20110048456 20110307
`(5):
`
`Also published aeaeaseia gee.)
`as:
`
`Abetract of JP2012183€331 tie}
`
`PRQBLEM TO BE SQLVED: To provide a method tor eiectrodiaiveia in order to
`tractionate and recover a ciuraiity oi kinds of acids from acideaccharitied iiquid, and an
`apparatus tor the eiectrodiaiyeia, used for such the method for the
`eiectrooiaivaia.SOLUTiON: By using the apparatus for the eiectrodiaiyeie, the oiuraiity
`of kinda of the acids are fractionated and recovered from the acid—saccharitied iiquid of
`ceiiniose~haeed hiornaes, At the apparatus for the eiectrodiaiysia a deeaiination
`chamber and a concentration chamber are inetaiied, and the concentration charriher ia
`divided into a first concentration chamber at a cathode side and a second concentration
`
`chamber in an anode side by an anion exchange membrane. At the deeaiination
`chamber, a deaaiinated saccharitied iiquid recovery pathway is: connected, and at the
`first concentration chamber, a first acid recovery pathway for recovering the acid having
`a tow permeation rate toward the anion exchanging membrane among the acids
`contained in the saccharitied iiauid in the deaaiination charnher is connected, and at the
`second concentration chamber, a second acid recovery pathway for recovering the acid
`having a high permeation rate toward the anion exchanging mernhrane is; connected.
`
`https://wor1dwide.espacenet. com/publicationDetails/biblio?II=O&ND=3&adj acent=true&loc. .. 2/8/2019
`
`
`
`Espacenet - Bibliographic data
`
`Page 2 of 2
`
`https://wor1dwide.espacenet. com/publicationDetails/biblio?II=O&ND=3&adj acent=true&loc. .. 2/8/2019
`
`
`
`2012183031-Desc-en
`
`Page 1 of 9
`
`Powered by EPI) 322:1 (Boogie
`
`Patent 123333131e
`
`T1215: 22321523220212 machinege2‘2e'2312321:tc3nn0I e r22I23n1eed tt‘a' it:s 221123129230 accurate complete 222231210 or-22212 2
`such as I.“ 31322221201321}; relevant or nuanciai decisions, shouid 2201 be based on Ina-.212Ede—223213132202": 2122222221.
`
`23:32"23221:: purposes. (321220231 decisions,
`
`
`
`I2123I21I2s 22':22I2 I221
`(:2352621311221C1 23222231 5:122:15;
`:22eI2'11223:1123132515 2:2:311222121 1:22' 5:223:223212Ig I22II2'
`PROBL 131211 TO 232?. SN..Vt—ED: 1:: provide I321
`acid g2yeated "quid end 321 e:eetredial‘,21ss so I-e3231225 us ed for r‘ar2y2ng 0221 5222311 an elest2c-di
`iysis method. I:SCILUT1C2N1 2n the
`I22'I:2sen1 222V::21tiI'-21, 231122222 2:112:35 2313I;i215 3223 s3I3II3II2, 322:1 reIo‘Iered 2'2'I22I2 3n soid g:'VII;I31ed-:'ioI22I1 I21 031i I22'o5iI 222022223555 by usi 21g
`322 electrodiaiyzer. The :22e231223I2'1231yzer is 21211122212321 2122112 23 21352311122123 2:22I22Iii>:22' and 3 23021233211223'122123 232132122332 and 11223 (2232223232212'I21ing
`chamber is d1212dec1 inte- e 1125-: concentrating chamber on the cathode side and :2 second ceneenhating ehan1be2‘ I222 the anode
`52:15 by I221 322:'on ::/:23hI3n:123 22'.- 2322113232223 ‘1':1:: de5I'2112n:2 1211222111232 15 CI-2‘:2'.-23I123d with :3 des3itedI2I2‘22I3221Id::2=:12d recovery 2322111,
`and 22112123 11251 2::2-:2I:::2I'1 2'23'22'2:1g:22322I'::-232.
`2322
`I2232221 12:3V2I2:; 3 2:22:12 23:22'222233222322223223 1221121 2:25;)3:2231 1:2 222:: anion exchange 2Iie22213223r2e
`among the acids contained in the saccharitied 53122222321
`in the deseit'i221g oompadmeht And a second acid recover}:2 path for
`223I:II2=ve22n:2 I322 acid having :2 his; 12 permeation rate to the anion 3XI;212221ge 222:2:“1113161128I15 CI~222223Ited tI21the 5e23232221 concentration
`23213232223321 (F18.
`
`Eieetredialysis method and electrsdieiysis appara1us
`
`{33313
`
`TECHMCAL HELD The present invention 2232:2tes to a method 12.22 5eI2I2rI2t2nI; I'2nd reeovedng 3 23iI2i'a222y I211<22221s 2313I2I15 120211 322
`
`
`ae1I13I30htai
`g 11I2=.22I2 such I35 an acid seocharit’ioeiion treatment 1123;221d which is a product obtaihed by saccharifying ce11uiesic
`biomass using 321 acid by e1eeti'edia2ysis, 321233" method To 321 e1eeti'edia2ysis appa23tu5 used to: 322 e=e231'dd232ys2s method for
`IeIzovew.
`
`{33322
`
`there is an attempt 223 31323121 ethano1 (bieethenoi) by deeomposéhg ceiiu2dse or
`As 3 2.23:: of biomass energy u122izetion,
`11::2112I;:3222.22I25:2. whioh is a main o23II1pI2he2Ito123ia21t5.
`
`12 is planned 12123'1tztie2I:-i23122eI2'::th221:21 is 22322152 h22xedi2'1he 23:21:222I:21>:'::2 122231 2I2I21211y for 12292 232 used as an 31191222312222: 12292 2232
`gesofine.
`
`{22212232
`
`1:5 23222232359 obiained 12y deoornposing
`2311122322222
`21223221 are 2332222205223, 222322212323111212359, herein 23: 512322312.
`The main (22322233213225 31211::
`cellulose. xy1ose obtaihed by decomposing hen12oe22uEI2se, seeoharides such as oligesacehemies which are commexes thereof
`A5 :3 23w 21133322222,
`it is produced by 121:: 1232'22223I21312on action 2312niI2'oor:23221sn2s 5:22:22 35 3223332.
`
`233343
`
`122 order 1:) decompose sellulosic biomass such as eel1221ose er hen12oe22uEI2se into saer‘1Is21Iie23,s a method (acid hydrolysis
`method) I2122ydr231yzi21g 132; I322 oxidizing power ofan 3:2:1 5= 2‘22 :35 phos I:- 21022:: I323:'d 232 512.1122212‘ I223221'is 2323222323213: used.
`
`http://translationporta1.epo.org/emtp/translate/?ACTION=description-retrieva1&COUNTRY. .
`
`. 2/8/20 1 9
`
`
`
`2012183031-Desc-en
`
`Page 2 of 9
`
`is preterabie to
`it
`in this acid hydroiysis method, since the added acid serves as an inhibitor against fermentation ct" yeast,
`
`decompose ceiiuicse or heniicelluicse into sacci .irides and then add the acid to ethanol
`,c-rior to ethnic-i fermentation of
`saccharides contained in the saccharit‘ied sciution Must be removed or neutraiized.
`
`{ones}
`
`Patent Document 1 discioses a technique of removing suituric acid in a saccharified solution by adding hydrated time to an acid
`saccharit’ied solution to neutraiize suituric acid and soiid~iiguid separating the formed gypsum. Here, it a strong acid added from
`the saocharit’ied solution can be recovered, a base for neutralization becomes unnecessary and cost can he reduced, but in the
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`method dis oised in Patent Document 1, suituric acid is regenerated front gypsum it is ditticuit to do.
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`{coca}
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`Cin the other hand, Patent Document 2 discioses a technique of tiowing an acid saocharit‘ied solution through an ion exchange
`resin to separate and recover suifuric acid. in addition, Patent Document 3 discloses an acid sacchariticaticn step of producing
`an acid / sugar mixture by subjecting ceiiuiosio biomass to acid saccharification treatment and a step ct using an anion
`exchange membrane for an acid i’ sugar mixture obtained from the acid saccharii‘ication step And a diaiysis treatment step of
`subjecting the acid and the sugar sciution to a diaiysis treatment by a diffusion diaiysis method at a temperature of 53 ° C or
`tees to produce a sugar solution from ceiiuiosic biomass . The method disciosed in Patent Document :3 is aimed at rnaidng it
`possibie to reo ver and reuse acid by using an ion exchange membrane and to reduce the energy cost and environmentai
`burden of the whoie process.
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`{cost}
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`Patent Document 1: JP 20967300? A Patent Document 2: 5? 26-35401 on A Patent Document 2: .JFLA 200922180
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`{coast
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`in the saccharitied solution, an organic acid {weak acid) which is a byproduct of ceiiuiose or hemiceliuiose saccharitication
`reaction is aiso contained.
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`Since the inorganic acid added in the sacchariticaticn step is high in concentration and expensive, it is preferable to recover the
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`inorganic acid from the saccharitied soiution and recycie it. i-iowever.
`.e the inorganic acid and the organic acid coexi
`(i the
`saccharit’ied soiution, when the inorganic acid mixed with the organic acid is
`reused in the sacchariticatic-n step,
`the
`concentration of the organic acid in the saccharitication stoc- increases. which adverseiy affects the saccharit‘ication step in
`addition to this, it aiso causes a rise in acid recovery cost, and furthermore. there is a probiem that the organic acid which can
`not he recovered hinders termentation in the subsequent termentation process.
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`goons}
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`On the other hand, with the methods disciosed in Patent Documents 2 and 3,
`piuraiity ct Kinds of acids contained in a saccharit‘ied soiutic-n.
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`it
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`is not possioie to separate and recover a
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`{onto}
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`ELD The present invention reiaies to an eiectrodiaiysis method t'cr separating and recovering saccharides and a
`TECi-iNECAL
`piuraiity oi kinds of acids from an acid saccharitied solution which is a product obtained by saccharifying ce" osic biomass with
`
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`an inorganic acid and a ntethcd for using such an electrod" iysis method And an object ofthe present invention is to provide an
`eiectrcdialyzer which is to be charged.
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`{cost}
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`The present inventors diiigently studied a method for separately recovering plurai kinds of acids from an acid-containing iiduid
`such as an acid saccharitied soiuticn.
`
`the
`in the eiectrodiaiyzer provided with the desaiting compartment and the concentrating compartment.
`As a resuit,
`concentrating compartment is divided by the anion exchange membrane, and the concentrating compartment is separated into
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`the desaiting compartment and the divided concentrating compartment by independent recovery routes ') To desaiinate the
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`saccharified solution, it is pc-ss ,.e to coiieet and recover pibral kinds of acids having different permeation rates with respect to
`the anion exchange membrane therebv compieting the present invention.
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`roots}
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`ent invention is a method of separating and recovering a piorality of kinds of acids from an acid-containing
`Specificaiiy, the or
`iidnid by eiec rodiaiysis. wherein the plnrai kinds of acids are different from each other in terms of a first acid And a second acid!
`wherein the rate of permeation of the first acid to the anion exchange membrane is tower than the rate of permeation of the
`second acid to the anion exchange membrane, sc- that the acid Passing the second acid from the cathode side to the anode
`side of the first anion exchange membrane, a second permeation step of passing the second acid from the cathode side to the
`anode side of the first anion exchange membrane, Through the second anion exchange membrane from the cathode side to the
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`anode side and permeates ihe first acid contained in ihe acid saccharificaiiori soiuticn from the cathode side of ihe iris anion
`exchange membrane to the anode side And a second transmission step
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`{oars}
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`it is preferable that the first acid is an organic acid and the second acid is an inorganic acid.
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`{core}
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`it is preferable that the acid~ccntaining iignid is an acid saccharified liquid of ce
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` m
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`roots}
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`The method of the present invention preferably has a recovery step of recovering the acid. saccharit’ied solution from which the
`first acid, the second acid, and the first acid and the second acid have been removed.
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`{cars}
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`it is preferable that the recovered second acid is reused in the acid saccharification step of ceildlcsic biomass
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`{port}
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`invention aiso provides an eiectrodialyser for separating and recovering plurai kinds of acids having different
`The present
`perrneaiicn rates ic sugar and anion exchange membrane contained in an acid saccharificaticn fr .atment soicticn of ceiiiiiosic
`biomass, wherein the electrodiaiyzer is provided with a desaiting chamber and a concentrating chamber, and a desalted
`saccharified iiduid recovery path is connected to the desalting compartment, and the concentrating compartment is connected to
`a desaitrng chamber at
`the cathode side having the anion exchange membrane between them A first concentrating
`compartment and a second concentrating compartment on the anode side, wherein the first concentrating compartment is
`provided with a first concentrating compartment for cc-iiecting the first acid having a tower permeation rate to the anion exchange
`membrane than the second acid A second acid recovery path for recovering the second acid having a higher permeation rate to
`the anion exchange membrane than the first acid is connected to the second concentration chamber, An eiectrodialyzer (first
`eiectrodialysis Device),
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`{core}
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`invention aiso provides an eiectrodialyzer for separating and recovering plLirai kinds of acids having different
`The present
`permeation rates with respect to sugar and anion exchange membrane contained in an acid sacch'iriticatien treatment solution
`of ceiiuiosic biomass, Wherein the acid comprises a first acid and a second acid having different permeation rates with respect
`to the anion exchange membrane, the eiectrodiaiyzer comprises a desalting compartment and a concentrating compartment, An
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`ion exchange membrane ., id corinecied w'th a desaited saccharified soirition recovery path, wherein the concentration chamber
`has a cation exchange membrane on the anode side and an anion exchange membrane on the cathode side. respectiveiyr A
`first concentrating chamber on the cathode side having an ion exchange membrane between each other and a second
`concentrating compartment on the anode side, wherein the first concentrating compartment is provided with a permeation
`membrane which permeates the anion exchange membrane The first acid recovery path for recovering the first acid having a
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`tower rate is in contact A second acid recovery path tor recovering the second acid having a higher permeation rate to the anion
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`exchange membrane than the first acid is connected to the second concentration chamber
`:altino the acidic saccharltied
`solution in the desaiting chamber and cciieoting the first acid and the second acid from the first acid recovery path and the
`second acid recovery path, respectiveiy , And an eiectrodiaiyzer (second eiectrodiaiyzer).
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`roots}
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`in the eiecirodiaiysis apparatns of the present invention. the concentration chamber is divided by an anion e