JPS59154981A - Biochemical conversion apparatus - Google Patents

Biochemical conversion apparatus

Info

Publication number
JPS59154981A
JPS59154981A JP59016921A JP1692184A JPS59154981A JP S59154981 A JPS59154981 A JP S59154981A JP 59016921 A JP59016921 A JP 59016921A JP 1692184 A JP1692184 A JP 1692184A JP S59154981 A JPS59154981 A JP S59154981A
Authority
JP
Japan
Prior art keywords
conduit
agent
biological
column
recovery device
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
JP59016921A
Other languages
Japanese (ja)
Inventor
チヤールズ・デイ・スコツト
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.)
US Government
Original Assignee
US Government
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 US Government filed Critical US Government
Publication of JPS59154981A publication Critical patent/JPS59154981A/en
Pending legal-status Critical Current

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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
    • C12P7/00Preparation of oxygen-containing organic compounds
    • C12P7/02Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/06Ethanol, i.e. non-beverage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Apparatus Associated With Microorganisms And Enzymes (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は、溶解(−7だ右別物!・1例えはiR’+
 ’a別な物質例λばアル−1−ルヘ転化りるlζめの
生物セγ・的転化”Ilξvqに関(JるものCある。 ■Φ/Zの叩出LJj、す、 lt生物学的、二誘jり
される転化反1.こ、lJJ、ニー)ζ人J、jl J
j、’H1,’−溶溶解6謀7′11\転化りる(19
1じマ(E糖をノフルIールl\Φλ化りる)ため(、
−は、バツ゛ヂ代シζ買(例えは5H酵1f!+)を−
用いる(了と(1適当(’ l’+−い、 t;Lつ(
従来l〕臼)、イJ(式1りj“1°°lの水id渣を
微イ1物を含むカー)ム(、−)中杭的じ流1ノ(この
右例物7′14別4r物71iにΦス化りることが提案
されでいる.、(この微生物を(二の四組It l!中
Cに1以後「/1物活I11剤1ど称tIイ)〉。溶M
? fj機別物1を他の物v11\転化りるlこめじt
lY来かf)用いら11 (い!、二連続流装置におい
ては、米IfL源ヲハ( )Jl.l 7 /7ターカ
ー> lxに19人1−7く/1物i+r11/1剤の
効力が<K クイ「らイr OJ、う(こ紺]′+□し
くいた。 この結T、かなりの半゛の栄11源をカラノ\(J添加
りることに4
This invention is a solution (-7 is a different thing! An example is iR'+
'A different substance example λ is converted into Al-1-R, lζ's biological body is concerned with the conversion of 'Ilξvq'. Target, two-tempered conversion anti-1.K, lJJ, knee) ζ person J, jl J
j, 'H1,'-dissolution 6 plot 7'11\conversion (19
1jima (to turn E sugar into nofur Il\Φλ) (,
- is buying a batch of ζ (for example, 5H fermentation 1f!+) -
Use (了と(1 appropriate('l'+-ii,t;L ツ(
Conventional l〕 mortar), IJ (Formula 1 rij "1°°l of water id residue containing fine A1 material) M(, -) Nakagashi style 1 no (this right example 7' It has been proposed to transform this microorganism into another 4r substance 71i. .Solution M
? fj special item 1 is converted to other item v11\comjit
lY come f) use 11 (I!, in two continuous flow devices, US IfL source wo ha ( ) Jl.l 7/7 Turker > lx 19 people 1-7/1 substance i+r11/1 efficacy of drug But <K Qui "Ray r OJ, U(kokon blue]' + □ was good. This result T, quite a half of Sakae 11 source was Karano\(J added) 4

【す、てのー)I)の多く(51利川さt
lること2r <通過しCしまう1、更に、過料の栄養
源物Y′1かカラムにM偵するど、カラム中の生物活性
剤の活性が減少覆る。 でこ(この発明0月1的は、illの如凸り別物Y′1
をアルコールの如き他の物質へ転化するためのJ、リ一
層効牢的な装置を提供覆ること(゛ある。 この発明の別な[1的は、連続流式操作ζ°しかも既知
装置においでは屡々認(ν)−ら;Il. i.− ;
、1物話・1ノi剤の活性低下のない、溶解右1幾物質
を他の物質l\転化りるための装置を提供りること−(
゛ある、。 −「記の目的を達成するため、この発明の生物学′的φ
l:化1−置は、 (’I) /、l物イi’i 11
1剤の生物活1イ1によって有機物質を別な物質へ転化
する主バイオリノア/)ター、(2)前記生物話j’l
剤のli物’6+ll’lを向1さIJろ回1昧2.!
器、ノZこ(J’ IC,)前記1バ(7Iすj/9)
I−ど回fsJ f?8どの間(前記生物話(/l剤4
11”j環さける装置どかIン+ !+’j +1V、
さit iイる、。 以[・に、添1・1図面(、二示した好まし7い実り旬
間を参照1.、、−(、、この発明を更(、−説明りる
。 第1図に(13いて、引用番号10は主バイAすj7ク
ターノノーノ!、を示り。この十カラ1)10の下端は
導7τ12によ・)も混合容器1/l(この混合容器は
この発明にと−)く不ロJ欠イ1しのCはない)の1喘
(、二If; t)c七さit、 (いる、、 ”!I
?Q”I 2 (、二設置J ”)れ(]いイインハル
フッ10こ、−1)((の)り管4流れるiAj体ノ2
m 吊−4’(1ill ill rl Zr 、、 
、A、 l I ’!1’i’、”I F’I ト出1
1導V。 20がこの自°器1/Iの側部じ+>iわ′Cさね讐い
る。。 この容器の下端(、ロ!ン釣22 +j 、−J、−、
(/l物活M剤の回復カラ!、2/l(以l・、回iu
器と称りる)の」一端l\接続され(いる。回復器のト
喘は、流量制御バルブ2Bを(悄λ〕、:導管−2Gに
よ−)て主バイA I)jツクターカラム10の」端に
1)1続さ41シいる。入1’:’l ’?:管30及
び出[l導管32はそれぞれ回復器2’lの下端及び上
端に接続され(イ13す、入口導管30はポンプ゛[〕
1へ接続されて、13す、出11導筑332は適当4丁
廃棄物排出装置へ接続されている。入[」導@3 /I
 a5よび出に1ン!J管36は同様にでれぞれカラム
10の下端d3 J、び、1端に接続されてd3す、入
口導管34はポンプP2へ18続されている。ン!Jγ
へ38は導τ112おJ、びポンプP3へ接続されてお
り、導管/10は導管26 J3J:びポンプP4へ接
続されている。 第2図に示づ別な実施例において、引用番号/12は主
バーイAリアクターカラムを示り。このjjプラム2の
下端は、導管46、ポンプP;)および導管48を介し
て、生物活性剤回j9カラ11・」なわJ)回tU器4
4の下端へ接続されでいる。 カラノ、712の1一端す聯↑14Gに接続された導管
50を介して回復器44へ接続されている。廃棄物導管
552は導管50から枝分かれしく−いる。 カラl\42の上端には、“つの出(−1府管54゜!
56 (> I!li t’にさね(いる11回復器4
 /I O,)−1端(ljよσ1・6+ル;は、ポン
プ゛[)にを備えた導管5862に4J、−)()】う
lX/I2のl;端へ接続され(いる、。 入11)り管(3/Iとポンプ1)7は導?τ62と接
続され、ムう つの入n ;rンT’; 66とポジ/
P8は導tへ55E3と接続さ4I、人11導悦6 F
3とポンプ])っけ回復器4/Iの下端ど接続され、i
J: I−’Il導管7072:J回復器の1喘ど接続
され(いる。 第1図Gj示し!、−この発明の実施1シ11の作タノ
を説明りると、J当41輪)Z流体く例えは11ζ)と
生物活性剤に、J、って別の/1−成物物7−1へ転化
されうるイj機¥1反応休どからイする流4′1が、ボ
ンf1)2によつ(+バイAリーj′クター10の下端
l\導入される。反応体どじ(は、△、 CO1l印旧
゛()どW。 G rifrill+ ’、’、” [valu旧io
n  or−311’、+ll’n1QRFor  1
3 ul;+nol   l″rotlucl ion
  °’  (1’)+;velol+m旧+Is  
 l l’l  l 11市+!l1rial  Nl
l icrobinlogy、  vat。 20 、  [7!l(1、3oet+!ly  fo
r   l n+luslria1Micro旧olO
!IV光行) ’k(”−it+311’k サ4’L
 (−イル、J、ライ「(Φ類の発酵しろろ水溶液を用
いることが
[Su, Teno] I) Many (51 Togawa Sat)
Furthermore, when the nutrient Y'1 of the grain is added to the column, the activity of the bioactive agent in the column is reduced. Deko (this invention October 1 is different from ill's convex Y'1
Another aspect of the present invention is to provide a more efficient apparatus for converting alcohol into other substances such as alcohol. Often recognized (ν)- et al; Il. i.-;
1. To provide an apparatus for converting a dissolved substance into another substance without reducing the activity of the agent.
Yes, there is. − “In order to achieve the stated purpose, the biological
l: chemical 1-position is ('I) /, l thingi i'i 11
The main biolinor that converts organic substances into other substances by the biological activity 1i1 of 1 agent /) ter, (2) The biological story j'l
Direction 1 and IJ rotation 1.2. !
Vessel, No Zko (J' IC,) Said 1ba (7Isuj/9)
I-How many times fsJ f? 8 Domo (the biological story (/l agent 4)
11"j ring avoidance device somewhere I + !+'j +1V,
It's okay. Hereinafter, the present invention will be further explained with reference to the attached drawings 1 and 1. The quotation number 10 indicates the main bias 1) The lower end of 10 is the lead 7τ12. (There is no C without 1)
? Q"I 2 (, 2 installation J ") Re(]iinhalhu 10 ko, -1) ((no) pipe 4 flowing iAj body no 2
m hanging-4'(1ill ill rl Zr,,
, A, l I'! 1'i',"I F'I to out 1
1st lead V. 20 is located on the side of this device 1/I. . The lower end of this container (,! Ron fishing 22 +j, -J, -,
(/lRecovery color of life active M agent!, 2/l (hereinafter referred to as l・, times iu
One end of the recuperator is connected to the main bypass column 10 by connecting the flow control valve 2B (by conduit 2G) to the main supply column 10. There are 1) 1 continuations at the end of 41. Enter 1':'l'? : The inlet conduit 30 and the outlet conduit 32 are connected to the lower and upper ends of the recovery device 2'l, respectively.
1, 13 and 11 are connected to an appropriate 4-tube waste discharge device. Enter ['' led @3 /I
A5 and 1n! J pipes 36 are similarly connected to the lower ends d3 and d3 of column 10, respectively, and inlet conduit 34 is connected to pump P2. hmm! Jγ
38 is connected to conduit τ 112 and pump P3, and conduit /10 is connected to conduit 26 J3J and pump P4. In the alternative embodiment shown in FIG. 2, reference number /12 designates the main Bay A reactor column. The lower end of this plumb 2 is connected to the bioactive agent via a conduit 46, a pump P;) and a conduit 48.
It is connected to the lower end of 4. It is connected to the recovery device 44 via a conduit 50 connected to one end of the Carano 712 and the other end 14G. A waste conduit 552 branches off from conduit 50. At the top of Kara l\42, there is a sign “Tsunode (-1 Fukan 54°!
56 (> I!li t' ni Sane (Iru 11 recovery device 4
/I O,)-1 end (lj as σ1.6+) is connected to the l; end of 4J,-)()] to l; . Is the inlet pipe (3/I and pump 1) 7 the lead? Connected to τ62, positive/
P8 connects with 55E3 to lead t 4I, person 11 lead 6F
3 and the pump]) is connected to the lower end of the recovery device 4/I, and
J: I-'Il conduit 7072: Connected to the first pipe of the J recovery device (as shown in Figure 1). Stream 4'1 from the reaction rest is injected into the tank, where the Z fluid (for example 11ζ) and the bioactive agent can be converted into another /1-product f1)2 is introduced into the lower end l\ of the reactor 10. io
n or-311', +ll'n1QRFor 1
3ul;+nol l″rotluclion
°'(1')+; velol+m old+Is
l l'l l 11 cities+! l1real Nl
l icrobinlogy, vat. 20, [7! l(1,3oet+!ly fo
r l n+luslria1Micro old olO
! IV Mitsuyuki) 'k ("-it+311'k sa4'L
(-Ile, J., Rai ``(It is possible to use fermented Shiroro aqueous solution of Φ class)

【−さる1゜カーラム10においη、(jl
幾質反1芯体は生物活IIl剤tel 、よつ(流(本
生酸物lX転化される。この生成物は)り管3Gから取
出される。、生物活性剤+、t r71分子右(幾物7
1の如さ・移動性粒状物(、二結含さ1!あ;j、> 
イル1%’、 i−’1 サ1.IC11す’ir。i
j4+ 7.> ’v’ ハjllH−,生物?1rl
f’l剤は、菌株の綿状沈降物(1スI(、フ1−lツ
クと称りる)の如き独S’7体としl ’L’、含さL
l /こリー含物(t、+ 、J、い。・二の装置の作
動の間(、−1輸送鑞体、活1〕14失−) 、、i=
 /、1物活i’l剤、it3よヒB !j3q 、’
/’i Js(応体(,1、〕」−ラlx 1 (1(
1−1・端から所i゛)111 r2にJ )(、連続
的;1−たIE周明白(X−抜出りむ=どが(−さる、
、 ;= l’tらの物V:+ t、+必要(二応(−
、: ’(、Qi、 fτ38か−)ンリ?τ12’\
添IJ11さ41ろItf1日)′、湧1本(IF、川
;t IJ71ζ)と11、(、−、ン1シ会容器14
 lX、送られる。駈?Y4「生物)、5牲剤おJ、σ
′また(、1301)++串の右1jt TT反I、ト
、体に1、う!仝管I E3を通し?iR含容器147
\添加づることかでき、ノ゛J、過ψりのノ1−物活1
゛1剤、13よびイ】(幾7゛j反Li・、、体は、導
i〜20によつC系から取出づこともでさる。。 生物活性剤、輸送流体おJ、び(j機道°1反応体は、
混合容器14 /)s rら導管22を通って回復器2
4の1一端へiXられる1、牛1υj活性剤の栄養源と
′/「る物7′1をう9筑30から回1!コjtjj 
2/Iド喘へ74人りる、。 回復器を通るイ1−物話lJI剤の流量は、パル716
(15よび28(Jよン(制御りる(二とが7−さ、2
1149話1′1剤が回復器内(J滞留しCいる間(、
二采f〜源物7′iにJ、・〉−(ノ1物活1’l剤は
1りび活1!l化さ4′する。必要ならば、’B lj
!t f’f反応反応体力加量を゛栄養源111、給ど
」((、−同m器24へ3υ入りる。ミとが1さる73
回+q シt、二11−物6’+ l:l剤(1、必要
C−1:iS;じに−)導管/10か+、’:、  5
−′??久 2  C’+  ’\  添 、1111
  ;\:I’l  Is  輸 )ス ンな1本 (
/、)  ;+3 JJll  串 ト」1、f;:、
Iハ(/11.17’Q勺−10のl !’iAi ’
\送+)、ltろ1゜このJ、 ’、> 1.−1.セ
、1ハイ4リノ′クク−1+−) 1人)(17) F
i l幾’i’(fil l:’1(1,) 牛、 1
4’2 物’\(1) 転化Fi 応f、、7 市41
 Z) 4物活1’l剤の!i「l 1i−t;L、こ
のシ′)、iノ、が連続的に1・■作へイ)、るこ、!
(1,J )(、定のレベルに糾合34°走る。 :’I! 2図に承し)こ(−の発明の別の実施例の作
動(、二おい(は、適当な輸)′A原流体イーi 1幾
r1反応体と/)”T>なる流IIが導管6’l、C3
2を通・)−(主バ、イ% l ;’り′)/I2 t
’1)1s ”n’Ii /\7j;+人さ1;ル1、
I ハ(71j、I ’7’ り4y−内1: CJ、
/1物括1’l剤/J” イ1tjlt Y’f F2
15体を流体)1成物l\転化12.この生成物(,1
、導τ′<54/)+ lろ取出される。輸’1.A 
rjii体、活性を失った生物8’r l’l剤A3 
J、び右im ?T 反応体く第2図中、Fl ’+ 
AC表わ()は連続的51ノこは周期的に導管/I6お
J、び50によ一部(主ハイAすiツクター/12の下
端まIJは」−喘1p +ろ取出りことがCき、S管/
16113Jびン7?管4Bを通り”で回1u器/l/
lの−に端または−1・端へ)スられる。主ハイAリア
クター42からの循環流の一部は、必要に応じ−(導管
52 b)61ノ[出さ1!ることもできる。失活した
生物活性剤のための栄養源kl: 、 j9管66にJ
ニー、)−(循環流/\添加され、)0加串の有機71
反応体と輸iM流体は導筑6ε3から回復器/14へン
綽人してちJ、い。 回復器44内で栄養源ににり回復した生物活性剤は、反
応体A3 J:び輸送流体と共にく第2図中、符号Bて
表わづ)、導管;う8,60.62から主ハイAリアク
ター712の1に喘へ戻される。過剰の物質は導管70
によってこの系から排出さ1+、ガスは導管72を通っ
C回復器44からtJr気される5、 b’321々11こ小しノ、1ハ(Aす/7り々−回復
器結、tylV、直′4用いC、ゲル−1−ス140す
′ρを含有・1 イ”)<iYr !内 41敢 ノ1
 棧ノ L、’  、j/)  反 1ト1、;、 (
iHl、(、/、 、  Il  物(米国国際j’i
!’ iU !;、!(門(あるjノグリカルrrラル
リリー−−1カルf−+7−  用1ノクシ」ン(△す
1゛1cullural  peseXIrcr+  
Cu1lure  (”、offection  )か
ら入「(さる、、)菌株ノ11ツノノを用い/:、: 
、、この試験装置の1バイΔすjツクター11: 、員
さ50CIllの重ii;1イrカー7ノ、からイTす
、内径1.27cmのカラムJ一端から内1¥lo、2
cmのカフ lx 下6X ;4: ’C’−j−パー
が−)lJられ(いる。三■:バーイイリ//クターノ
ノラノ、には、□L県旦ユl モヒ臥入の同定菌株の直
i予約0.5にm・・・2.Oc…の゛)「lツクが含
有され(A3す、この)11ツクは+バイAすjJり々
−にお(」る流動床ど<@−)’U J:;す、一方供
給溶液はこの流Φ;ノ床を通しく流1>るJ、うになっ
ている1、主ハイAリアクターb 51\は長さ30c
mの回復器カラムJ:j巾通さIJ、との値11党薄力
ラ11は内1子1.27cmの下幅1から内fM 2 
、4i Il c mのl、−4AQ t\と7−バー
かつ()られている。循1■水溶液A3.J、びぞの中
(こ懸)蜀されηいイ)オ°1ン゛1入り゛イ■しノス
 しヒ去ンは、1バ(Aリノ′ツノクーの底部から回復
器の頂部l\ど移動し、螺動ポン/にJ、−、>−(回
復器の底部から↑へ−(Aクツ′クターの旧都へど戻さ
れる1、試験操作の間に、クルー1−1λ含右供給溶i
ff に「IバYΔリアクターの1部へ導入され、米j
1源含イj溶?iシ(,1回復器の1部へ導入されイ)
1、i記の流動床へり反応装置M L;I: 、グルー
1−ス140geを含有りる供にIl水)γfifkを
12…O′分(供給i)ること(、二J、: −) (
、最初(、−作動4開始さけた。。 十ハーイΔりj′クタ−内1.゛萌n12のり一、イし
七ノス旦よ−u、3ユ菌株ハ1ツクが形成される第1 
r!>階の間 、 FIIl句 11./’!5   
リ ′ ρ 、  (Nll)SO’142L    
4 す・′ρ、Ml  、’304・7 It、00.!′
IIIeオJ、ひK 1lzP 04 1  !I ′
、Q ヲrk tIVl ロ’l? M 河i水fFf
 !f!li ’6−前記グルーI−klFF液と」(
(3二1バイAすj′クタ−(λ、フE1ツクが1−バ
イオリアクター内にかなりの■蓄(hさ]lだのち、前
記栄養源fFY液の供給を1宇+l−1−1、主バイA
リアクターカラム内Cグルー1−スの丁タノールおよび
一酸化炭素への生物的転化反応が壁定常状態に達りるま
C、グルニI−ス水溶液02主バイΔリシ′クターへの
供給を継続した。主バ、イAリアクターへの栄養源の導
入を停止づると、カラノ、内で・の転化案は40)間以
内でかなり減少し、2/1時間以内て−はこのカラム(
J栄養源を添IJII L、 (いる111の1l17
. lヒ十の10%以十の1ノベルに達し1.Xoごの
1111点ζ、す(、IEt)スーーーg景−+ノーノ
ー 、ノ11ツクの回194器力−ンムl\の循圀と」
゛バイ、4 ’、J 、j’り々−への戻しを間&j’
i シ、グルレー ス2 (’l  !+ 、’ 、Q
おJ、σ1記L)、−一二同L”+’+’! !!’j
の栄m 1tiaケ含む栄笹源供給溶6を2 mO分の
割合(回11jz器力)ノ、σ用戊部ノ\向11.’+
 1.−4l rr? l−+ 7.:、この1已−ド
(−技同):il、 51Ri間1午千)jさIJると
、1バr7づりj′りう一内(−A 1/lノノル1−
λの一1ツノノールl\の生物的転化件It、 t−3
09(o 1.スII!1加し/、: 、、 1’ ハ
4ΔすIり))  内(0)/l物転化十11ξの1(
J1°1加し続(J、栄11源4−グルーゴーーーλ供
治液流と共f、、ニー1バ(、eリノ7クク一へ導入し
I、:とさの3き入1,11合の1イ・かl−17%程
嗅の)#、 A Pt’lI 白(パl’、j、l’H
貯iyダ渋4回it、>汁31\導入し、 1:: M
もがl]叫J ”’> ’J” 、 生物1irl性f
in ’ffi I”11(l器/\循1■さlq /
7が) /、Hl+、’lの転化;fの6111°11
ス1のし・ベルに達した。7(lのことがら、Jの発明
に、1、る/L物学的転化゛に買の作動りI+ :tが
極め(1・Qれ(いることがわかる。 1、図161の簡1”+7説明 第1図はこの発明(こJ、るバー1’ Aリアクター装
置の実施例を示りd(明図Cあり、第2図(5Lこの翔
明のバ(Aリノ′クター装勧の別4r実施例を示・J説
明図(ある。 10・・・主バイΔリアクタ〜、12・・・生物活性剤
1厚応体(15J、び輸送流体循環用導管、21・・・
回復器、2G・・・回1121−・た〈1物活1′1剤
1反I芯1ホお、よび輸送流体用導管1.3o・・・栄
養源J3よび、′または反応仕入]二1導宣、332・
・・廃東物出1゛1カ質、3’l・・・反応体おJ、び
輸送流体入1]1導管、36・・・流(4,〈1−成物
出1」導管。
[-Monkey 1° Kalam 10 η, (jl
The polygonal monocore body is converted into bioactive agent IlX. This product is taken out from tube 3G. Bioactive agent +, t r71 molecule right (Kimono 7
1-like/mobile particulate matter (, 2-containing 1!A;j,>
il1%', i-'1 sa1. IC11S'ir. i
j4+ 7. > 'v' HajllH-, living thing? 1rl
The f'l agent is a flocculent sediment of the bacterial strain (referred to as F1-ltsuk), which contains German S'7 bodies, l'L', and L'L'.
l/Collie inclusion (t, +, J, i. During the operation of the second device (, -1 transport brazing body, active 1] 14 loss -),, i =
/, 1 thing life i'l agent, it3 yohi B! j3q,'
/'i Js(respond body(,1,]"-ra lx 1 (1(
1-1・From the end to i゛) 111 r2 to J) (, continuous;
, ;= l't et al.'s V: + t, + necessary (two corresponding (-
,: '(, Qi, fτ38?-) Nri? τ12'\
Attachment IJ11sa41roItf1day)', 1 spring (IF, river; t IJ71ζ) and 11, (, -, n1shi meeting container 14
lX, sent. Canter? Y4 “biology), pentagonal agent OJ, σ
'Also (, 1301) ++ 1 jt to the right of the skewer TT anti-I, t, 1 to the body, uh! Through IE3? iR container 147
\Addition can be made, ノ゛J, excess ψ no 1 - living life 1
Agents 1, 13 and A) (7) anti-Li, bodies can also be removed from the C system by conduction i~20. Bioactive agents, transport fluids, and ( jKido°1 reactant is
Mixing vessel 14 /) s r et al through conduit 22 to recovery vessel 2
IX to one end of 4, 1, cow 1υj activator nutritional source and '/'/'ru thing 7'1 from 9 Chiku 30 times 1! Kojtjj
74 people to 2/I do pant. The flow rate of the JI agent through the recovery device is 716
(15 and 28
Episode 1149 1'1 While the drug stays in the recovery device (J and C (,
J, ・〉-(No1 life 1'l agent is 1 life life 1!l 4'. If necessary, 'B lj
! t f'f reaction reaction physical strength addition ``nutrient source 111, feed'' ((, - 3υ enters the same m vessel 24.
times + q site, 211- thing 6' + l: l agent (1, required C-1: iS; di-) conduit / 10 or +, ':, 5
−′? ? Ku 2 C'+ '\ So, 1111
;\:I'l Is import) Sun na one book (
/,) ;+3 JJll skewer 1,f;:,
Iha (/11.17'Q勺-10のl!'iAi'
\Transmission+), ltro1゜This J, ', > 1. -1. Se, 1 high 4 reno'kuku -1+-) 1 person) (17) F
i l'i'(fil l:'1(1,) cow, 1
4'2 Things'\(1) Conversion Fi,,7 City41
Z) 4 things 1'l agent! i ``l 1i-t;L, this shi'), iノ, are continuously 1・■worked), Ruko,!
(1, J) (, run 34 degrees at a fixed level. :'I! Refer to Figure 2) Operation of another embodiment of this (-) invention (, 2 (, suitable import)' A raw fluid E i 1 some r 1 reactant and/) ”T> Stream II flows through conduit 6'l, C3
2 through) - (main bar, i% l;'ri')/I2 t
'1) 1s "n'Ii /\7j; + person sa 1; le 1,
I Ha (71j, I '7' ri 4y-1: CJ,
/1 substance 1'l agent/J" I1tjlt Y'f F2
15 bodies into fluid) 1 compound l\conversion 12. This product (,1
, the lead τ'<54/)+l is extracted. Import'1. A
rjii body, organism that has lost activity 8'r l'l agent A3
J, right im? T reactant In Figure 2, Fl '+
The AC display () is continuous 51 times the conduit / I6 and J, and 50 part (the lower end of the main high A filter / 12 or IJ) is 1p + filtration. C, S tube/
16113J bottle 7? Pass through tube 4B and turn 1u/l/
(to the - end or -1 end of l). A portion of the circulating flow from the main high-A reactor 42 is optionally supplied to the outlet 1! You can also Nutrient source kl for deactivated bioactive agent: , J to J9 tube 66
Knee,) - (circulating flow/\added,) 0 kake skewer organic 71
The reactant and fluid are transferred from the 6ε3 to the recovery device/14. The bioactive agent recovered in the nutrient source in the recovery vessel 44 is transferred to the reactant A3 (represented by reference numeral B in FIG. It is returned to 1 of the high A reactor 712. Excess substance is transferred to conduit 70
1+ gas is exhausted from this system through conduit 72 and discharged from C recovery device 44. , Direct '4 use C, Gel-1-su 140su'ρ containing 1 ')<iYr !
棧ノL、'、j/)Anti 1ト1、;、(
iHl, (, /, , Il thing (US International j'i
! 'iU! ;、! (1 noxine for (1)
Entered from Cu1lure (",offection) "(Saru,,)Using strain No. 11 Tsunono/:,:
,,The weight of this test device is 11: 1 column is 50 CIll; 1 column is 7 mm;
cm cuff lx lower 6X M ... 2. OC… ゛…… ゛) “L -Tsuku is included (A3, this) 11 Tsuku is + Bai A JJ Ririsa (@-- )'U J: ;, while the feed solution flows through this flow Φ;
m restorer column J: j width through IJ, and value 11 party thin force la 11 is 1 child 1.27 cm lower width 1 to inner fM 2
, 4i Il cm l, -4AQ t\ and 7-bar and (). Circulation 1 ■ Aqueous solution A3. J, the inside of the hole is closed. 1, during the test operation, the crew 1-1 λ included melting
ff was introduced into a part of the I-YΔ reactor, and rice j
Does it contain 1 source? i (introduced into one part of the recovery device)
1. The fluidized bed reactor M L; ) (
, first (, - the operation 4 was started. 1. 12 times in the 1st period, 1st time when the 3rd bacterial strain cluster was formed)
r! > Between floors, FIIl phrase 11. /'! 5
ri ′ ρ , (Nll) SO'142L
4 Su・'ρ, Ml, '304・7 It, 00. ! ′
IIIe OJ, HiK 1lzP 04 1! I'
,Q work tIVl ro'l? M river i waterfFf
! f! li'6-the glue I-klFF liquid and'' (
(321by A sj' vector (λ, 1) After a considerable amount of accumulation (h) l in the bioreactor, the supply of the nutrient fFY liquid is increased by 1 u+l-1- 1. Main by A
The aqueous solution of C and Glunice was continued to be supplied to the main bi-Δresictor until the biological conversion reaction of C and Glue to ethanol and carbon monoxide in the reactor column reached a wall steady state. . When the introduction of nutrients to the main reactor is stopped, the conversion rate in the column decreases considerably within 40 hours, and within 2/1 hour the column (
Add J nutrient source IJII L, (111 of 1l17
.. 1. Reach 1 novel in 10% or more of 10 times. Xo Go's 1111 points
゛Bye, 4', J, j'Return to Riri- while &j'
i shi, guru race 2 ('l !+ ,' ,Q
OJ, σ1ki L), -12 L”+'+'!!!'j
The ratio of 2 mO of the Sakae source supply solution 6 containing the Sakae m 1tia (11jz force) for σ is 11. '+
1. -4l rr? l-+ 7. :, this 1 已-do (-technical same): il, 51 Ri between 1 hour 1,000) j sa IJ, 1 bar r7 spelling j' Riuichi (-A 1/l nonor 1-
Biological transformation of λ11Tunonol l\ It, t-3
09 (o 1.SII!1 addition/,: ,, 1' HA4ΔSuri)) Inside (0)/l material conversion 111ξ 1 (
J1°1 addition (J, Sakae 11 source 4-Glugo-λ together with liquid flow f,, knee 1 bar (, e Reno 7 Kuku 1 I,: Tosa no 3 entry 1, 11 points of 1-17% smell) #, A Pt'lI White (Pl', j, l'H
Save iy dashibu 4 times, > juice 31\ introduced, 1:: M
struggle] shout J ”'>'J', biological 1irl sex f
in 'ffi I"11 (l device/\circulation 1 ■ sa lq/
7) /, Hl+, 'l conversion; 6111°11 of f
Reached the first bell. 7 (Concerning l, it can be seen that in J's invention, 1, R/L physical transformation, I + : t is the ultimate (1 · Q). 1, Simplified 1 of Fig. 161 +7 Explanation Figure 1 shows an embodiment of the A reactor device of this invention. 10... Main biΔreactor ~, 12... Bioactive agent 1 thick reaction body (15J, and transport fluid circulation conduit, 21...
Recoverer, 2G...times 1121-・(1 material activity 1' 1 agent 1 anti-I core 1 hole, and transport fluid conduit 1.3o...nutrient source J3 and 'or reaction supply) 21 guidance, 332.
...Waste product output 1゛1 substance, 3'l... Reactant and transport fluid input 1] 1 conduit, 36... Flow (4, <1-product output 1'' conduit.

Claims (1)

【特許請求の範囲】[Claims] 1、イ1物ン1!l性剤の生物活性によ−)で11機物
質を別な物質へ転化リ−る土バイAリアクターと、前記
勺物活(’l剤の生物活性を向上さける回復器と、前記
主バイΔリアクターと回復器との間で前記どl物活竹剤
を循環さμる%同どからなる生物学的転化装置。
1, 1 thing, 1! A soil biological reactor that converts 11 substances into other substances by the biological activity of the biological agent, a recovery device that improves the biological activity of the biological agent, and a recovery device that improves the biological activity of the biological agent. A biological conversion device consisting of the same amount of recycled bamboo material as described above between the Δreactor and the recovery vessel.
JP59016921A 1983-02-08 1984-02-01 Biochemical conversion apparatus Pending JPS59154981A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US46483883A 1983-02-08 1983-02-08

Publications (1)

Publication Number Publication Date
JPS59154981A true JPS59154981A (en) 1984-09-04

Family

ID=23845449

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59016921A Pending JPS59154981A (en) 1983-02-08 1984-02-01 Biochemical conversion apparatus

Country Status (4)

Country Link
JP (1) JPS59154981A (en)
BR (1) BR8400494A (en)
DE (1) DE3403607A1 (en)
GB (1) GB2134540A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991009110A1 (en) * 1989-12-15 1991-06-27 Kirin Beer Kabushiki Kaisha Continuous fermentation process and reactor therefor

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB401495A (en) * 1931-11-19 1933-11-16 Dansk Gerings Ind As Process for producing spirits by fermentation of materials containing carbohydrates
GB393082A (en) * 1932-02-12 1933-06-01 Melle Usines Sa Improvements relating to the alcoholic fermentation of sugarcontaining liquids
GB1087307A (en) * 1965-05-31 1967-10-18 Inst Die Gaerungs Und Getraenk Process and apparatus for the continuous fermentation and maturing of beer
GB1160297A (en) * 1966-08-10 1969-08-06 Inst Die Gaerungs U Getraenkei Method and Apparatus for the Accelarated and Continuous Fermentation and Maturation of Beerwort
GB1262186A (en) * 1969-05-17 1972-02-02 Forsch Die Gaerungsindustrie E Method and apparatus for continuous fermentation and maturing of beer wort
CA1174191A (en) * 1980-03-05 1984-09-11 Peter L. Rogers Ethanol production

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1991009110A1 (en) * 1989-12-15 1991-06-27 Kirin Beer Kabushiki Kaisha Continuous fermentation process and reactor therefor

Also Published As

Publication number Publication date
BR8400494A (en) 1984-09-11
GB2134540A (en) 1984-08-15
GB8401731D0 (en) 1984-02-22
DE3403607A1 (en) 1984-08-09

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