JPH062077B2 - Method of measuring cell concentration - Google Patents
Method of measuring cell concentrationInfo
- Publication number
- JPH062077B2 JPH062077B2 JP5578286A JP5578286A JPH062077B2 JP H062077 B2 JPH062077 B2 JP H062077B2 JP 5578286 A JP5578286 A JP 5578286A JP 5578286 A JP5578286 A JP 5578286A JP H062077 B2 JPH062077 B2 JP H062077B2
- Authority
- JP
- Japan
- Prior art keywords
- cell concentration
- bacterial cell
- treatment
- measuring
- liquid
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 14
- 230000001580 bacterial effect Effects 0.000 claims description 27
- 239000007788 liquid Substances 0.000 claims description 21
- 238000000855 fermentation Methods 0.000 claims description 16
- 230000004151 fermentation Effects 0.000 claims description 16
- 238000005259 measurement Methods 0.000 claims description 14
- 235000018102 proteins Nutrition 0.000 claims description 11
- 102000004169 proteins and genes Human genes 0.000 claims description 11
- 108090000623 proteins and genes Proteins 0.000 claims description 11
- 230000005284 excitation Effects 0.000 claims description 9
- 238000004519 manufacturing process Methods 0.000 claims description 9
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 7
- 230000007928 solubilization Effects 0.000 claims description 7
- 238000005063 solubilization Methods 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 3
- 235000004252 protein component Nutrition 0.000 claims description 2
- 230000001678 irradiating effect Effects 0.000 claims 1
- 230000003381 solubilizing effect Effects 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 244000005700 microbiome Species 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000012262 fermentative production Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 241000202987 Methanobrevibacter Species 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 230000000696 methanogenic effect Effects 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 235000013555 soy sauce Nutrition 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 241000228212 Aspergillus Species 0.000 description 1
- 241000228245 Aspergillus niger Species 0.000 description 1
- 240000006439 Aspergillus oryzae Species 0.000 description 1
- 235000002247 Aspergillus oryzae Nutrition 0.000 description 1
- 241000131386 Aspergillus sojae Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- QIVBCDIJIAJPQS-VIFPVBQESA-N L-tryptophane Chemical compound C1=CC=C2C(C[C@H](N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-VIFPVBQESA-N 0.000 description 1
- 229930182555 Penicillin Natural products 0.000 description 1
- JGSARLDLIJGVTE-MBNYWOFBSA-N Penicillin G Chemical compound N([C@H]1[C@H]2SC([C@@H](N2C1=O)C(O)=O)(C)C)C(=O)CC1=CC=CC=C1 JGSARLDLIJGVTE-MBNYWOFBSA-N 0.000 description 1
- 241000228150 Penicillium chrysogenum Species 0.000 description 1
- QIVBCDIJIAJPQS-UHFFFAOYSA-N Tryptophan Natural products C1=CC=C2C(CC(N)C(O)=O)=CNC2=C1 QIVBCDIJIAJPQS-UHFFFAOYSA-N 0.000 description 1
- 238000002835 absorbance Methods 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 239000003242 anti bacterial agent Substances 0.000 description 1
- 229940088710 antibiotic agent Drugs 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229940049954 penicillin Drugs 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000007925 protein solubilization Effects 0.000 description 1
- 238000001799 protein solubilization Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- GPRLSGONYQIRFK-MNYXATJNSA-N triton Chemical compound [3H+] GPRLSGONYQIRFK-MNYXATJNSA-N 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Investigating, Analyzing Materials By Fluorescence Or Luminescence (AREA)
- Investigating Or Analysing Materials By The Use Of Chemical Reactions (AREA)
- Measuring Or Testing Involving Enzymes Or Micro-Organisms (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は微生物による発酵生産あるいは生物反応による
生物処理を行う生物反応槽におけるメタン菌その他の菌
体濃度を簡便かつ正確に測定することができる菌体濃度
の測定方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention can easily and accurately measure the concentration of methane bacteria and other cells in a biological reaction tank in which fermentation production by a microorganism or biological treatment by a biological reaction is performed. The present invention relates to a method for measuring bacterial cell concentration.
(従来の技術) 微生物の働きにより有用物質を生産する発酵生産や下廃
水中の有機性汚濁物質(BOD)を好気性菌や嫌気性菌
等の菌体により処理する生物学的処理においては、生物
反応槽内の菌体濃度を正確に知ることが運転管理上非常
に重要である。そこで従来の生物学的処理においては、
処理槽内の微生物量の代表値としてMLSS(全懸濁汚
泥量)という概念を導入してこのMLSS又はMLVS
S(全有機性懸濁物質)を測定することにより運転管理
が行われているが、これらの値は溶液中の浮遊性物質を
全て含んでいるため処理すべき下廃水に伴って入ってく
る菌体以外の物質によって影響され、菌体濃度を正確に
把握するには不正確な値と言うべきである。しかもML
SSの測定は20分間の遠心分離、沈澱物への加水を複
数回繰返したうえ蒸発乾固、2時間乾燥、デシケータ中
で放冷等の手順で行うべきことが下水試験法によって定
められており、MLVSSの測定にはこのほか更に60
0℃で30〜40分間の強熱減量が必要であるので、測
定に4〜10時間という長い時間を必要とする欠点があ
った。(Prior Art) In the fermentation treatment for producing useful substances by the action of microorganisms and the biological treatment for treating organic pollutants (BOD) in wastewater with aerobic bacteria and anaerobic bacteria, Accurately knowing the bacterial cell concentration in the bioreactor is very important for operation management. So in conventional biological processing,
Introducing the concept of MLSS (total suspended sludge volume) as a representative value of the amount of microorganisms in the treatment tank, this MLSS or MLVS
Operation control is performed by measuring S (total organic suspended solids), but these values come in with the wastewater to be treated because they contain all floating substances in the solution. It is affected by substances other than bacterial cells and should be called an inaccurate value in order to accurately grasp the bacterial cell concentration. Moreover, ML
The sewage test method stipulates that the SS measurement should be carried out by repeating the procedure of centrifugation for 20 minutes, water addition to the precipitate several times, evaporation to dryness, drying for 2 hours, and cooling in a desiccator. , 60 more for MLVSS measurement
Since the ignition loss is required at 0 ° C. for 30 to 40 minutes, there is a drawback that the measurement requires a long time of 4 to 10 hours.
一方微生物を用いた有用物質の発酵生産分野でも事情は
同様である。確かに、酢酸発酵等基質が溶解性で生産物
も溶解性、しかも使用する微生物が、発酵液中に均一分
散するバクテリアの場合には、発酵槽内の菌体濃度は、
発酵液中に分散浮遊した菌体濃度に比例する吸光度(Op
tical Density:O.D.)で測定可能であるが、通常の発酵
生産においては、このO.D.では菌体濃度を測定できない
場合が多い。例えば 抗生物質(例えばペニシリン)の発酵生産に使用され
るカビ類(例えばPenicillium chrysogenum)あるい
は、クエン酸発酵に使用されるカビ類(Aspergillus ni
ger)の様に菌糸状発育をする菌については、菌自身が
からみ合いフロックを作る為O.D.を使っての菌体濃度測
定は不可能となる。現在は前述のMLSSを測定するの
と同様の方法で乾燥菌体重量を測定し菌体濃度の指標と
しているが、前述同様その測定には時間がかかりオンラ
イン制御の指標とすることは不可能である。On the other hand, the situation is similar in the field of fermentative production of useful substances using microorganisms. Certainly, when the substrate such as acetic acid fermentation is soluble and the product is also soluble, and the microorganism used is a bacterium that is uniformly dispersed in the fermentation broth, the bacterial cell concentration in the fermentor is
Absorbance (Op
It is possible to measure the bacterial cell concentration with this OD in normal fermentation production. For example, molds (eg Penicillium chrysogenum) used for fermentative production of antibiotics (eg penicillin) or molds used for citric acid fermentation (Aspergillus ni
Germ-like bacteria, such as ger), make it impossible to measure bacterial cell concentration using OD because the bacteria themselves entangle and form flocs. Currently, the dry microbial cell weight is measured by the same method as the above-mentioned MLSS measurement and used as an index of the microbial cell concentration, but as with the above, the measurement takes time and cannot be used as an index for online control. is there.
しょう油発酵生産においてはやはりカビ類(Aspergil
lus oryzae,Aspergillus sojae、etc)がその発酵生産
に関与しその菌体濃度は、やはり上述の如く乾燥菌体重
量で代表している。しかしこのしょう油の発酵生産にお
いては事情はさらに複雑である。すなわち発酵原料とし
て大豆等固形物を使用している為乾燥菌体として測定さ
れる乾燥固形物のかなりの部分はこの発酵原料由来の固
形物であり従って菌体濃度の測定は非常に不正確なもの
であった。In soy sauce fermentation production, molds (Aspergil
lus oryzae, Aspergillus sojae, etc.) are involved in the fermentation production, and the cell concentration is represented by the dry cell weight as described above. However, the situation is more complicated in the fermentative production of soy sauce. That is, since a solid material such as soybean is used as a fermentation raw material, a large part of the dried solid matter measured as dry bacterial cells is solid matter derived from this fermentation raw material, and therefore the measurement of the bacterial cell concentration is very inaccurate. It was a thing.
(発明が解決しようとする問題点) 本発明はこのような従来の問題点を解決して、生物反応
槽中の菌体濃度を正確にしかも短時間に測定することが
できる菌体濃度の測定方法を目的として完成されたもの
である。(Problems to be Solved by the Invention) The present invention solves such conventional problems and enables measurement of bacterial cell concentration in a biological reaction tank accurately and in a short time. It was completed for the purpose of the method.
(問題点を解決するための手段) 本発明は発酵生産用の発酵槽あるいは生物処理用の生物
処理槽等の生物反応槽から引抜いた生物反応槽内液に蛋
白質可溶化剤を添加して可溶化処理を施したのち懸濁物
質を除去する固液分離処理を行い、その分離液に所定波
長の励起光線を照射して分離液中の蛋白成分が発する蛍
光の強度を測定することを特徴とするものである。(Means for Solving Problems) The present invention allows the addition of a protein solubilizer to a biological reaction tank liquid extracted from a biological reaction tank such as a fermenter for fermentation production or a biological treatment tank for biological treatment. After performing the solubilization treatment, a solid-liquid separation treatment for removing suspended matter is performed, and the separation liquid is irradiated with an excitation light having a predetermined wavelength to measure the intensity of fluorescence emitted by the protein component in the separation liquid. To do.
本発明においては、先ず生物反応槽から引抜かれた生物
反応槽内液に蛋白質可溶化剤を添加して可溶化処理が行
われる。蛋白質可溶化剤としてはトリトン系の可溶化剤
をはじめ多くのものが存在するが、SDS(ドデシル硫
酸ナトリウム)が最も有効であり、好ましくは予想され
る菌体濃度の2〜20倍の濃度のSDSが添加される。
これ以下の添加量では蛋白質の可溶化が不十分で蛍光強
度と菌体量との間に満足な相関関係が得られないおそれ
があるからである。ここで予想される菌体濃度としては
MLSS又はMLVSSの10〜50%程度の値を採用
すればよく、予備測定を一度行えばSDSの妥当な添加
量が確認できる。可溶化処理においては可溶化を促進す
るためSDS等の添加された生物反応槽内液を80〜1
00℃で5〜10分間加熱処理することが好ましく、測
定条件を揃えるためには100℃で例えば10分間煮沸
処理することが好ましい。しかし加熱時間を長くとれば
これ以下の温度でも差支えない。このような蛋白質の可
溶化処理の結果、生物反応槽内液中の菌体の主成分であ
る蛋白質が液中に溶出するので、次に液中から懸濁物質
を除去するための固液分離処理を行う。固液分離処理は
例えば3000rpm×20分間の遠心分離処理を行え
ば十分であるが、濾紙による濾過でもよく、これによっ
て下廃水に伴ない生物処理槽中に入ってくる砂などの無
機物及び有機繊維などの夾雑物を分離する。このように
して菌体から溶出した蛋白質を含有し、夾雑物が除去さ
れた分離液が得られるので、次にこの分離液に対して、
蛍光分光光度計を用いて所定波長の励起光線を照射す
る。励起光線の波長を260〜320nm、より好まし
くは280〜300nmとしたとき、分離液からは34
0nmに極大波長を持ち第1図に示すように320〜3
80nmの波長範囲に分布する蛍光が生ずるのでこれを
測定する。測定された蛍光強度は後の実施例にも示すと
おり生物反応槽内液中の菌体濃度と1次相関を持つこと
が確認され、この蛍光強度の測定によって菌体濃度を正
確に把握することができる。なお、メタン生成菌により
生物処理を行わせる場合にはメタン発酵反応の電子伝達
系に関与する酵素であるF420が420nmの励起波長に
よって励起され470nm近傍の蛍光を発することが知
られているが、本発明の測定対象となる蛍光はピーク波
長及び蛍光強度のいずれにおいてもF420による蛍光とは
明らかに相違するものであり、トリプトファンのような
蛋白由来のものであることが確認された。In the present invention, first, a solubilization treatment is carried out by adding a protein solubilizing agent to the liquid inside the biological reaction tank drawn from the biological reaction tank. There are many protein solubilizers including triton solubilizers, but SDS (sodium dodecyl sulfate) is most effective and preferably has a concentration of 2 to 20 times the expected concentration of cells. SDS is added.
This is because if the amount added is less than this, the protein may be insufficiently solubilized and a satisfactory correlation between the fluorescence intensity and the amount of cells may not be obtained. As the bacterial cell concentration expected here, a value of about 10 to 50% of MLSS or MLVSS may be adopted, and an appropriate addition amount of SDS can be confirmed by performing preliminary measurement once. In the solubilization treatment, in order to promote solubilization, the biological reaction tank liquid to which SDS or the like has been added is adjusted to 80 to 1
It is preferable to perform heat treatment at 00 ° C. for 5 to 10 minutes, and to make the measurement conditions uniform, it is preferable to boil at 100 ° C. for 10 minutes, for example. However, if the heating time is long, it does not matter if the temperature is lower than this. As a result of such protein solubilization treatment, the protein, which is the main component of the bacterial cells in the liquid in the biological reaction tank, is eluted into the liquid.Next, solid-liquid separation is performed to remove suspended substances from the liquid. Perform processing. For the solid-liquid separation treatment, for example, centrifugation treatment at 3000 rpm × 20 minutes is sufficient, but filtration with filter paper may also be used, whereby inorganic substances such as sand and organic fibers that enter the biological treatment tank with the wastewater are introduced. Separate contaminants such as. In this way, the separated solution containing the protein eluted from the bacterial cells and freed from contaminants is obtained.
A fluorescence spectrophotometer is used to irradiate excitation light of a predetermined wavelength. When the wavelength of the excitation light is 260 to 320 nm, more preferably 280 to 300 nm, it is 34
It has a maximum wavelength of 0 nm and as shown in FIG.
Fluorescence distributed in the wavelength range of 80 nm is generated and is measured. It was confirmed that the measured fluorescence intensity had a first-order correlation with the bacterial cell concentration in the liquid in the biological reaction tank, as will be shown in the following examples, and the bacterial cell concentration should be accurately grasped by measuring this fluorescent intensity. You can It is known that F 420, which is an enzyme involved in the electron transfer system of methane fermentation reaction, is excited by an excitation wavelength of 420 nm and emits fluorescence in the vicinity of 470 nm when biological treatment is performed by a methanogen. The fluorescence to be measured in the present invention is clearly different from the fluorescence by F 420 in both peak wavelength and fluorescence intensity, and it was confirmed that it was derived from a protein such as tryptophan.
(実施例) 実施例1 グルコース、酢酸、蟻酸等によって2〜3月馴養を続け
たメタン生成菌(メタノブレビバクターアーボリフィラ
ス A2、Methanobrevibacter arboriphilas)を含む嫌
気性の生物処理槽(消化温度37℃)から生物処理液を
引抜き、予想される菌体濃度の2〜20倍のSDSを添
加したうえ100℃で10分間煮沸して可溶化処理を行
った。これを3000rpm×20分間の遠心分離器に
よる固液分離処理を行い、得られた分離液に蛍光分光光
度計を用いて波長290nmの励起光線を照射し、測定
波長340nmで蛍光強度を測定した。この結果、第2
図に白丸で示すようにMLSSとして別途測定された菌
体濃度と蛍光強度との間に強い相関があることがわかっ
た。なお同時に励起波長420nm、測定波長470n
mとしてF420の発する蛍光強度をも測定したところ、第
2図に黒丸で示すとおりの結果が得られ、メタン生成菌
の濃度についてはF420の場合にもやはり相関が成立する
ことがわかった。しかしF420の蛍光強度は比較的弱いう
えに、好気性の生物処理槽のようにメタン生成菌以外の
菌体を用いる場合にはF420は存在せず、本発明方法によ
ってはじめて菌体濃度の正確な測定が可能となる。(Example) Example 1 An anaerobic biological treatment tank containing a methanogenic bacterium (Methanobrevibacter arbophilus A2, Methanobrevibacter arboriphilas) kept acclimatized with glucose, acetic acid, formic acid, etc. for 2 to 3 months (digestion temperature 37 ° C) ), The biological treatment solution was drawn out, SDS of 2 to 20 times the expected bacterial cell concentration was added, and the mixture was boiled at 100 ° C. for 10 minutes for solubilization treatment. This was subjected to solid-liquid separation treatment with a centrifuge at 3000 rpm for 20 minutes, and the obtained separated liquid was irradiated with excitation light having a wavelength of 290 nm using a fluorescence spectrophotometer, and the fluorescence intensity was measured at a measurement wavelength of 340 nm. As a result, the second
As indicated by white circles in the figure, it was found that there is a strong correlation between the bacterial cell concentration separately measured as MLSS and the fluorescence intensity. At the same time, the excitation wavelength was 420 nm and the measurement wavelength was 470 n.
When the fluorescence intensity emitted from F 420 was also measured as m, the results shown by the black circles in FIG. 2 were obtained, and it was found that the correlation also holds for the concentration of methanogens in the case of F 420 . . However, the fluorescence intensity of F 420 is relatively weak, and F 420 does not exist when cells other than methanogenic bacteria are used, such as in an aerobic biological treatment tank. Accurate measurement is possible.
なお、比較のために生物処理液をアセトン処理、トルエ
ン処理、超音波処理したうえで同様に蛍光強度を測定し
たが、トルエン処理した場合には無処理と同様にほとん
ど蛍光が測定できず、またアセトン処理及び超音波処理
したものは蛍光が測定されたが蛍光強度は本発明の方法
による場合に比較してはるかに小さかった。For comparison, the fluorescence intensity was measured in the same manner after treating the biological treatment solution with acetone, toluene, and ultrasonic waves, but when treated with toluene, almost no fluorescence could be measured as in the untreated case, and Fluorescence was measured in the acetone-treated and sonicated ones, but the fluorescence intensity was much smaller than that obtained by the method of the present invention.
実施例2 発酵生産に使用される代表的なカビの一種であるアスペ
ルギルス ニガー(Aspergillus niger)を培養し、その
乾燥菌体濃度と本発明による蛍光強度について相関を見
た。Example 2 Aspergillus niger, which is one of the typical molds used for fermentation production, was cultured and the correlation between the dry cell concentration and the fluorescence intensity according to the present invention was observed.
乾燥菌体濃度と、実施例1と同一方法で測定した本発明
による蛍光強度の時間変化とをプロットした結果を第3
図に示す。第3図のグラフからわかる様に、黒丸で示さ
れた乾燥菌体濃度と白丸で示された蛍光強度の間には強
い相関がありカビを使った発酵生産においても、本発明
の方法により、菌体濃度が簡便に測定できることがわか
った。The results of plotting the concentration of dry cells and the time change of the fluorescence intensity according to the present invention measured by the same method as in Example 1 are shown in Table 3.
Shown in the figure. As can be seen from the graph of FIG. 3, there is a strong correlation between the dry cell concentration shown by the black circles and the fluorescence intensity shown by the white circles, and even in the fermentation production using mold, the method of the present invention It was found that the cell concentration can be easily measured.
(発明の効果) 本発明は以上の説明からも明らかなように、菌体の主成
分が蛋白質であることに着眼し、これを可溶化処理した
うえ固液分離して夾雑物を除き、分離液に所定波長の励
起光線を照射して蛋白由来の蛍光を発生させてその強度
を測定することにより菌体濃度を知るものであるから、
従来のMLSSを測定する方法に比較して菌体濃度のみ
を正確に測定することができ、しかも測定に要する時間
をMLSSの測定を行う場合の1/4以下の1〜2時間
にまで短縮することができる。よって本発明によれば嫌
気性、好気性のいずれの生物処理方法においても、また
発酵生産においても生物反応槽内液中の菌体濃度の測定
を簡便かつ正確に行うことができ、その運転管理の適正
を期するために極めて有益である。(Effect of the invention) As is apparent from the above description, the present invention focuses on the fact that the main component of bacterial cells is a protein, solubilizes this, and then solid-liquid separates to remove impurities, Since the liquid is irradiated with excitation light of a predetermined wavelength to generate fluorescence derived from protein and the intensity thereof is measured, the bacterial cell concentration is known.
Compared with the conventional method for measuring MLSS, only the bacterial cell concentration can be measured accurately, and the time required for the measurement is shortened to 1 to 2 hours, which is ¼ or less of the time required for measuring MLSS. be able to. Therefore, according to the present invention, in any of the anaerobic and aerobic biological treatment methods, and also in the fermentation production, it is possible to easily and accurately measure the bacterial cell concentration in the liquid in the biological reaction tank, and to manage its operation. It is extremely useful for ensuring the appropriateness of.
第1図は本発明方法において測定された蛍光波長と蛍光
強度との関係を示すグラフ、第2図は第1の実施例にお
ける菌体濃度と蛍光強度との関係を示すグラフ、第3図
は第2の実施例における乾燥菌体濃度と蛍光強度との関
係を示すグラフである。FIG. 1 is a graph showing the relationship between fluorescence wavelength and fluorescence intensity measured in the method of the present invention, FIG. 2 is a graph showing the relationship between bacterial cell concentration and fluorescence intensity in the first example, and FIG. 3 is It is a graph which shows the relationship between a dry cell density | concentration and a fluorescence intensity in a 2nd Example.
Claims (4)
生物処理槽等の生物反応槽から引抜いた生物反応槽内液
に蛋白質可溶化剤を添加して可溶化処理を施したのち懸
濁物質を除去する固液分離処理を行い、その分離液に所
定波長の励起光線を照射して分離液中の蛋白成分が発す
る蛍光の強度を測定することを特徴とする菌体濃度の測
定方法。1. A solubilizing treatment by adding a protein solubilizing agent to a liquid in a biological reaction tank drawn from a biological reaction tank such as a fermenter for fermentation production or a biological treatment tank for biological treatment, followed by suspension. A method for measuring a bacterial cell concentration, which comprises performing a solid-liquid separation treatment for removing a substance, and irradiating the separated liquid with an excitation light having a predetermined wavelength to measure the intensity of fluorescence emitted by a protein component in the separated liquid.
の2〜20倍の濃度のSDS(ドデシル硫酸ナトリウ
ム)を用いる特許請求の範囲第1項記載の菌体濃度の測
定方法。2. The method for measuring the bacterial cell concentration according to claim 1, wherein SDS (sodium dodecyl sulfate) having a concentration of 2 to 20 times the expected bacterial cell concentration is used as the protein solubilizer.
め80〜100℃で5〜10分間の加熱処理を行う特許
請求の範囲第1項記載の菌体濃度の測定方法。3. The method for measuring the bacterial cell concentration according to claim 1, wherein in the solubilization treatment, heat treatment is carried out at 80 to 100 ° C. for 5 to 10 minutes in order to promote solubilization.
り、蛍光測定波長が320〜380nmである特許請求
の範囲第1項記載の菌体濃度の測定方法。4. The method for measuring the bacterial cell concentration according to claim 1, wherein the wavelength of the excitation light is 260 to 320 nm and the fluorescence measurement wavelength is 320 to 380 nm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5578286A JPH062077B2 (en) | 1986-03-13 | 1986-03-13 | Method of measuring cell concentration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5578286A JPH062077B2 (en) | 1986-03-13 | 1986-03-13 | Method of measuring cell concentration |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62210999A JPS62210999A (en) | 1987-09-17 |
| JPH062077B2 true JPH062077B2 (en) | 1994-01-12 |
Family
ID=13008466
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5578286A Expired - Lifetime JPH062077B2 (en) | 1986-03-13 | 1986-03-13 | Method of measuring cell concentration |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH062077B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4867413B2 (en) * | 2006-03-20 | 2012-02-01 | 栗田工業株式会社 | Evaluation method and apparatus for reverse osmosis membrane feed water and operation management method for water treatment apparatus |
-
1986
- 1986-03-13 JP JP5578286A patent/JPH062077B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62210999A (en) | 1987-09-17 |
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