WO2006075030A2 - Biosensor for determining the biochemical oxygen demand (bod) by respirometry - Google Patents
Biosensor for determining the biochemical oxygen demand (bod) by respirometry Download PDFInfo
- Publication number
- WO2006075030A2 WO2006075030A2 PCT/EP2006/050235 EP2006050235W WO2006075030A2 WO 2006075030 A2 WO2006075030 A2 WO 2006075030A2 EP 2006050235 W EP2006050235 W EP 2006050235W WO 2006075030 A2 WO2006075030 A2 WO 2006075030A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- biosensor
- respirometry
- capsules
- measurement system
- water
- Prior art date
Links
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims description 26
- 229910052760 oxygen Inorganic materials 0.000 title claims description 26
- 239000001301 oxygen Substances 0.000 title claims description 26
- 239000002775 capsule Substances 0.000 claims abstract description 28
- 244000005700 microbiome Species 0.000 claims abstract description 10
- 230000037452 priming Effects 0.000 claims abstract description 8
- 238000005259 measurement Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 claims description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 239000002028 Biomass Substances 0.000 claims description 14
- 230000003213 activating effect Effects 0.000 claims description 8
- 239000011159 matrix material Substances 0.000 claims description 7
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 6
- 241000894006 Bacteria Species 0.000 claims description 4
- 239000001110 calcium chloride Substances 0.000 claims description 4
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 4
- 108010050327 trypticase-soy broth Proteins 0.000 claims description 4
- 239000003643 water by type Substances 0.000 claims description 3
- FHVDTGUDJYJELY-UHFFFAOYSA-N 6-{[2-carboxy-4,5-dihydroxy-6-(phosphanyloxy)oxan-3-yl]oxy}-4,5-dihydroxy-3-phosphanyloxane-2-carboxylic acid Chemical group O1C(C(O)=O)C(P)C(O)C(O)C1OC1C(C(O)=O)OC(OP)C(O)C1O FHVDTGUDJYJELY-UHFFFAOYSA-N 0.000 claims 3
- 229940072056 alginate Drugs 0.000 claims 3
- 235000010443 alginic acid Nutrition 0.000 claims 3
- 229920000615 alginic acid Polymers 0.000 claims 3
- 239000000499 gel Substances 0.000 claims 3
- 230000035899 viability Effects 0.000 claims 2
- 238000013461 design Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 description 17
- 239000000523 sample Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 4
- 238000012544 monitoring process Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 3
- 230000036284 oxygen consumption Effects 0.000 description 3
- 230000001988 toxicity Effects 0.000 description 3
- 231100000419 toxicity Toxicity 0.000 description 3
- 235000013361 beverage Nutrition 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000011065 in-situ storage Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000011368 organic material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000012086 standard solution Substances 0.000 description 2
- IXPNQXFRVYWDDI-UHFFFAOYSA-N 1-methyl-2,4-dioxo-1,3-diazinane-5-carboximidamide Chemical compound CN1CC(C(N)=N)C(=O)NC1=O IXPNQXFRVYWDDI-UHFFFAOYSA-N 0.000 description 1
- 101100049727 Arabidopsis thaliana WOX9 gene Proteins 0.000 description 1
- 241000588914 Enterobacter Species 0.000 description 1
- 101150059016 TFIP11 gene Proteins 0.000 description 1
- 102100032856 Tuftelin-interacting protein 11 Human genes 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000012512 characterization method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000002198 insoluble material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 238000009629 microbiological culture Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 235000010413 sodium alginate Nutrition 0.000 description 1
- 239000000661 sodium alginate Substances 0.000 description 1
- 229940005550 sodium alginate Drugs 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N11/00—Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof
- C12N11/02—Enzymes or microbial cells immobilised on or in an organic carrier
- C12N11/04—Enzymes or microbial cells immobilised on or in an organic carrier entrapped within the carrier, e.g. gel or hollow fibres
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/18—Water
- G01N33/1806—Biological oxygen demand [BOD] or chemical oxygen demand [COD]
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/18—Water
- G01N33/186—Water using one or more living organisms, e.g. a fish
- G01N33/1866—Water using one or more living organisms, e.g. a fish using microorganisms
Definitions
- the present invention is related with the environmental characterization of liquid residue, as much as what refers to control and monitoring activities, as of treatment, more specifically with a biosensor for determining the biochemical oxygen demand (BOD) by respirometry.
- BOD biochemical oxygen demand
- the BOD is an important index for the organic pollution monitoring in liquids, therefore, is an indirect measure of the amount of organic material in liquids, in general and in water in particular , that can be biologically degraded by microorganism , since the dissolved oxygen get consumed during the degradation biochemical process of the organic material , then the said oxygen quantity can be expressed in equivalent form in terms of the quantity of required oxygen (respirometry), thus, the BOD is capable of identify in a quantitative way the degradable charge existing in residual water or in a body receptor.
- the biosensor consists on a combination of a transducer and a biological element, for example as microorganism and oxygen electrodes (see fig. 1).
- the on-line measurement systems consist basically in an unity (membrane or bioreactor), populated of microorganism (that can be specific of the liquid to be monitored) in which a continuous flow is maintained through a recirculating pump, being feed by peristaltical pumps that load the residual liquid simultaneously other pump saturates of oxygen the monitoring liquid (recipient fixed to the equipment or system), and a probe for the measurement of dissolved oxygen. This measurement can be made with different configurations.
- respirometric activity register of the microorganisms in a reactor is used, which are extracted in a little quantity (aliquot) from a chemostat.
- STIP ISCO GmbH has a biosensor named biox 1010, for the measurement of the content of BOD and toxicity in an automatic form waters of different origin.
- the method used is respirometric, based on a microbial culture coming from the water to be monitored that gradually deposits over insoluble supports inside the reactor (EP 0369490), whose composition, concentration and activity are constant. It metabolizes the organic matter of the samples such that consumed oxygen for it oxidation allows to know the BOD and toxicity values.
- the apparatus and method previously described have the difficult of containing a limited quantity of biomass that reduces the range of measurement to waters with low BOD. Is the case of those that use membranes supported over the oxygen sensor. On the other hand those based on microorganism supported over insoluble material, must be generated in situ over the base of the bacteria present in the liquid to be monitored making impossible design the microbiological load of the reactor and requiring priming time of many days that must be repeated every time that the bio film get deteriorated because of use or toxicity.
- Figure 1 shows a general scheme of the constitutive parts of biosensors.
- FIG 2 shows the diagram of the system that measure BOD using the present invention.
- Figure 3 shows the Cartridge type removable bioreactor (BTC) of the present invention.
- Figure 4 shows a typical respirometric curve, indicating the distinct zones of respirometric activity.
- Figure 5 shows the results of a calibration BOD obtained in the laboratory versus the resulting respirometric area for each experiment using a standard solution.
- Figure 6 shows the results of a calibration BOD obtained in the laboratory versus the resulting respirometric area for each experiment using an effluent (RIL) solution coming from an industry.
- the present invention provides a system that operates like a biosensor, for the fast measurement of DBO, where the apparatus used as respirometric element is a cartridge type removable and disposable bioreactor (BTC)(I), in which the biomass is encapsulated in a polymeric organic matrix suspended in a support solution which, in the preferred modality is calcium chloride.
- BTC cartridge type removable and disposable bioreactor
- the BTC (1) has in every moment an inlet (40) and outlet (41) of support liquid, that comes from a recipient (2) that stores this support liquid.
- the circulating pump (4) maintains a constant flow, that is to say, the input and output flow are equal, while the liquid volume is constant inside of the BTC on every moment.
- the output support liquid is discarded, and can go to the drainage or other outlet (6), also has on every moment an air flow intake (50), that after bubbling discharges to the atmosphere (51).
- a sample which is obtained from an aliquot of the canals, rivers or lakes (RILES) (7), inside the BTC (1) trough a second inlet (70).
- the injected sample is pulse type (the whole sample is injected at a time).
- the BTC Before injecting the sample, the BTC is acquiring data from the dissolved oxygen sensor (200) to an acquiring data equipment, inside zone 1 (see figure 4), configuring a first base line.
- the dissolved oxygen data begins to drop down , because of the injection of the sample coming from RIL (7) , which marks the beginning of zone 2 denominate dissolved oxygen consumption zone. Then the dissolved oxygen begins to rise, which marks the beginning of zone 3 denominated dissolved oxygen recuperating zone. After a few minutes, the dissolved oxygen data get stabilized which indicates that a new base line is established, zone 4, in this way the BTC is ready for monitoring another sample to be injected.
- the dissolved Oxygen consumption and recovery zones data are selected, that is to say zones 2 and 3, where they are numerically integrated to obtain a first area under the curve (A 1 ).
- Zones 1 and 4 are worked with the data of the respective base lines. An interpolation is done creating a theoretical base line corresponding to the dissolved oxygen consumption zone (zone 2) and the dissolved oxygen recovery zone (zone 3). The theoretical base line is integrated with which a second area under the curve is obtained (A 2 ).
- Respirometric area mL A 2 -A 1
- the evaluation of BOD can be done of different forms, one way is comparing the Respirometric Area ML versus the respirometric area of Standard or known values of DBO measured previously.
- Figure 5 shows the results of a BOD calibration obtained on laboratory versus the resulting respirometric area for each experiment using a liquid standard solution. The data is on table 1.
- Figure 6 illustrates the method for measuring BOD on real RILES samples coming from a beverage industry; data is shown on table 2.
- the cartridge type bioreactor (BTC) has an immobilized quantity of biomass on capsules (100), which was previously generated, that means, we have a preexistent biomass quantity that can be adjusted to the capsule (100), the capsule size (100) is also adjustable within certain limits, while the capsules number is also adjustable to the BTC size (1). All this indicates that the operation characteristics of the removable and disposable BTC (1) can be adjusted to the user requirements.
- the BTC priming or activating time is less than the commercial alternatives available today, this prime or activating time goes from 4 hours to 1 day.
- the BTC (1) is constructed from a cartridge of inert material with adapters for: inlet for feeding the support solution (40), outlet of liquid (41), measurement sample inlet (70), air inlet (50), air outlet (51), dissolved oxygen sensor (200) that in a preferred modality is removable. Additionally contains the capsules suspended on storing liquid or in support liquid when is in operation.
- the capsule forming solution consist on 1% sodium alginate where a population of bacteria Enterobacter sakasakii was introduced and previously homogenized and formerly isolated from residual water until reaching to a microbial concentration of 0.5 grams dry biomass /liter of capsule. This solution was dropped from the capsule device to a hardening solution of calcium chloride, 0.05 molar, generating capsules on the order of 1 millimeter diameter.
- the capsules were stored cold on trypticase soy (TSY) solution diluted on calcium chloride 0.05 molar solution.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Biomedical Technology (AREA)
- Zoology (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Biotechnology (AREA)
- Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Dispersion Chemistry (AREA)
- Medicinal Chemistry (AREA)
- Analytical Chemistry (AREA)
- Food Science & Technology (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Emergency Medicine (AREA)
- General Engineering & Computer Science (AREA)
- Biodiversity & Conservation Biology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Immobilizing And Processing Of Enzymes And Microorganisms (AREA)
Abstract
A removable cartridge that contains an adjustable number of capsules inside of which there are adjustable masses of immobilized microorganisms, allowing the design of a simple apparatus and the use of a reactor with less priming times. Reactors of this type can be stored in cold allowing the replacement of the operating reactor easily.
Description
BIOSENSOR FOR DETERMINING THE BIOCHEMICAL OXYGEN DEMAND (BOD) BY RESPIROMETRY
FIELD OF THE INVENTION
The present invention is related with the environmental characterization of liquid residue, as much as what refers to control and monitoring activities, as of treatment, more specifically with a biosensor for determining the biochemical oxygen demand (BOD) by respirometry.
BACKGROUND OF THE INVENTION
The BOD is an important index for the organic pollution monitoring in liquids, therefore, is an indirect measure of the amount of organic material in liquids, in general and in water in particular , that can be biologically degraded by microorganism , since the dissolved oxygen get consumed during the degradation biochemical process of the organic material , then the said oxygen quantity can be expressed in equivalent form in terms of the quantity of required oxygen (respirometry), thus, the BOD is capable of identify in a quantitative way the degradable charge existing in residual water or in a body receptor.
Depending on temperature conditions, other nutrients availability and absence of inhibitors, the whole degradation process takes normally about 20 days. As a partial analytic measure, but statistically representative of the organic charge of a liquid residue, a conventional method denominated BOD5 has been used that consist in incubating the sample for 5 days at 200C, However this is a method that although is normalized, it is complicated and above all it duration of 5 days for quantifying the BOD does not allows to take opportune and efficient operational actions.
Consequently with the former, different types of biosensors have been developed based on respirometry and also associated methods that allows to know the BOD in situ and on real time , and obtain this measurement in a simple and fast form (in the order of minutes).
The biosensor consists on a combination of a transducer and a biological element, for example as microorganism and oxygen electrodes (see fig. 1).
The on-line measurement systems consist basically in an unity (membrane or bioreactor), populated of microorganism (that can be specific of the liquid to be monitored) in which a continuous flow is maintained through a recirculating pump, being feed by peristaltical pumps that load the residual liquid simultaneously other pump saturates of oxygen the monitoring liquid (recipient fixed to the equipment or system), and a probe for the measurement of dissolved oxygen. This measurement can be made with different configurations.
By example immobilized microorganism on polyacrylamide gel and a oxygen electrode are used ("A rapid method for estimation of BOD by using Microbial Cells", Isao Karube and els., Biotechnology and Bioengineering VoI XIX , p.1535-1547, 1977).
Also the respirometric activity register of the microorganisms in a reactor is used, which are extracted in a little quantity (aliquot) from a chemostat.
STIP ISCO GmbH has a biosensor named biox 1010, for the measurement of the content of BOD and toxicity in an automatic form waters of different origin. The method used is respirometric, based on a microbial culture coming from the water to be monitored that gradually deposits over insoluble supports inside the reactor (EP 0369490), whose composition, concentration and activity are constant. It metabolizes the organic matter of the samples such that consumed oxygen for it oxidation allows to know the BOD and toxicity values.
The apparatus and method previously described have the difficult of containing a limited quantity of biomass that reduces the range of measurement to waters with low BOD. Is the case of those that use membranes supported over the oxygen sensor. On the other hand those based on microorganism supported over insoluble material, must be generated in situ over the base of the bacteria present in the liquid to be monitored making impossible design the microbiological load of the reactor and requiring priming time of many days that must be repeated every time that the bio film get deteriorated because of use or toxicity.
In the case of apparatus based on feed from a chemostat, the operative requirements make necessary a great number of feeding pumps, empty, air, recirculation and wash generating highly complex equipment, sharing the limiting of priming time
SUMMARY OF THE INVENTION
In the actual invention this problems are approached and for giving a solution it is proposed a removable cartridge that contains an adjustable number of capsules inside of which there are adjustable masses of immobilized microorganisms, allowing the design of a simple apparatus and the use of a reactor with less prime times. Reactors of this type can be stored in cold allowing the replacement of the operating reactor easily.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 (previous art), shows a general scheme of the constitutive parts of biosensors.
Figure 2 shows the diagram of the system that measure BOD using the present invention. Figure 3 shows the Cartridge type removable bioreactor (BTC) of the present invention.
Figure 4 shows a typical respirometric curve, indicating the distinct zones of respirometric activity.
Figure 5 shows the results of a calibration BOD obtained in the laboratory versus the resulting respirometric area for each experiment using a standard solution.
Figure 6 shows the results of a calibration BOD obtained in the laboratory versus the resulting respirometric area for each experiment using an effluent (RIL) solution coming from an industry.
DETAILED DESCRIPTION OF EMBODIMENTS OF THE INVENTION
In this way, the present invention provides a system that operates like a biosensor, for the fast measurement of DBO, where the apparatus used as respirometric element is a cartridge type removable and disposable bioreactor (BTC)(I), in which the biomass is encapsulated in a polymeric organic matrix suspended in a support solution which, in the preferred modality is calcium chloride.
As shown in figure 2, the BTC (1) has in every moment an inlet (40) and outlet (41) of support liquid, that comes from a recipient (2) that stores this support liquid. The circulating pump (4) maintains a constant flow, that is to say, the input and output flow are equal, while the liquid volume is constant inside of the BTC on every moment. The output support liquid is discarded, and can go to the drainage or other
outlet (6), also has on every moment an air flow intake (50), that after bubbling discharges to the atmosphere (51).
In order to start the measurement, it is necessary to inject a sample, which is obtained from an aliquot of the canals, rivers or lakes (RILES) (7), inside the BTC (1) trough a second inlet (70). The injected sample is pulse type (the whole sample is injected at a time).
Before injecting the sample, the BTC is acquiring data from the dissolved oxygen sensor (200) to an acquiring data equipment, inside zone 1 (see figure 4), configuring a first base line. As shown on drawing 4, and when the sample is injected , the dissolved oxygen data begins to drop down , because of the injection of the sample coming from RIL (7) , which marks the beginning of zone 2 denominate dissolved oxygen consumption zone. Then the dissolved oxygen begins to rise, which marks the beginning of zone 3 denominated dissolved oxygen recuperating zone. After a few minutes, the dissolved oxygen data get stabilized which indicates that a new base line is established, zone 4, in this way the BTC is ready for monitoring another sample to be injected.
Once the data is obtained, the dissolved Oxygen consumption and recovery zones data are selected, that is to say zones 2 and 3, where they are numerically integrated to obtain a first area under the curve (A1).
Zones 1 and 4 are worked with the data of the respective base lines. An interpolation is done creating a theoretical base line corresponding to the dissolved oxygen consumption zone (zone 2) and the dissolved oxygen recovery zone (zone 3). The theoretical base line is integrated with which a second area under the curve is obtained (A2).
To calculate the "Respirometric area" the resulting areas must be subtracted according to:
Respirometric areamL = A2 -A1
The evaluation of BOD, can be done of different forms, one way is comparing the Respirometric Area ML versus the respirometric area of Standard or known values of DBO measured previously.
„ -^ Respirometric areamr „
BOD = — Factor
Respirometric areaSTAmARD
Other way is comparing the Respirometric area ML versus a calibrated curve previously constructed with standard known BOD solutions.
BOD = f {Respirometric area)
Figure 5 shows the results of a BOD calibration obtained on laboratory versus the resulting respirometric area for each experiment using a liquid standard solution. The data is on table 1.
TABLE 1: BOD calibration obtained on laboratory
Figure 6 illustrates the method for measuring BOD on real RILES samples coming from a beverage industry; data is shown on table 2.
TABLE 2: BOD measure on RILES samples of a beverage industry
The cartridge type bioreactor (BTC) has an immobilized quantity of biomass on capsules (100), which was previously generated, that means, we have a preexistent biomass quantity that can be adjusted to the capsule (100), the capsule size (100) is also adjustable within certain limits, while the capsules number is also adjustable to the BTC size (1). All this indicates that the operation characteristics of the removable and disposable BTC (1) can be adjusted to the user requirements.
The BTC priming or activating time is less than the commercial alternatives available today, this prime or activating time goes from 4 hours to 1 day.
The BTC (1) is constructed from a cartridge of inert material with adapters for: inlet for feeding the support solution (40), outlet of liquid (41), measurement sample inlet (70), air inlet (50), air outlet (51), dissolved oxygen sensor (200) that in a preferred modality is removable. Additionally contains the capsules suspended on storing liquid or in support liquid when is in operation.
EXAMPLE
The capsule forming solution consist on 1% sodium alginate where a population of bacteria Enterobacter sakasakii was introduced and previously homogenized and formerly isolated from residual water until reaching to a microbial concentration of 0.5 grams dry biomass /liter of capsule. This solution was dropped from the capsule device to a hardening solution of calcium chloride, 0.05 molar, generating capsules on the order of 1 millimeter diameter.
For constructing the BTC, 20 grams of capsules suspended on 40 cc of support liquid were used, consisting in a calcium chloride solution 0.05 molar.
The capsules were stored cold on trypticase soy (TSY) solution diluted on calcium chloride 0.05 molar solution.
Claims
1. A respirometry biosensor for fast determination of BOD (Biochemical Oxygen Demand) in water's flow wherein it consists on a BTC (Cartridge type reactor) removable, with a quantity of biomass immobilized on capsules and a removable dissolved oxygen sensor.
2. The respirometry biosensor according to claim 1, wherein the capsules are suspended on a solution.
3. The respirometry biosensor according to claim 2, wherein the solution is calcium chloride when the biosensor operates.
4. The respirometry biosensor according to claim 2, wherein the solution is a broth of trypticase soy (TSY) in calcium chloride solution, when the capsules are stored.
5. The respirometry biosensor according to claim 2 wherein the capsules are gels that contains bacteria and a polymeric organic matrix.
6. The respirometry biosensor according to claim 5, wherein the polymeric organic matrix is an alginate based solution.
7. The respirometry biosensor according to claim 6, wherein the capsules are adjustable on number and/or size and/or contents.
8. The respirometry biosensor according to claim 7, wherein the capsule contents are adjustable to the characteristics of the water to be monitored.
9. The respirometry biosensor according to claim 8, wherein the characteristics of the water to be monitored determinates the quality and quantity of organic load.
10. The respirometry biosensor according to claim 9, wherein the waters to be monitored are coming from Industrial plants, rivers, lakes or canal (RILES).
11. The respirometry biosensor according to claim 1 , wherein further the BTC is disposable.
12. The respirometry biosensor according to claim 1, wherein the biomass quantity immobilized on capsules is previously generated.
13. The respirometry biosensor according to claim 12, wherein the biomass quantity immobilized on the capsules is stored in cold, maintaining the viability of the microorganisms.
14. The respirometry biosensor according to claim 13, wherein the priming or activating time of the BTC is at least 4 hours.
15. The respirometry biosensor according to claim 14, wherein the priming or activating time of the BTC is no longer than 24 hours.
16. Respirometric measurement system for fast obtaining of BOD (Biochemical Oxygen Demand) on water's flow, wherein it comprises a removable biosensor, with a quantity of immobilized biomass in gels capsules that contains bacterias and an organic polymeric matrix and a removable dissolved oxygen sensor.
17. The respirometric measurement system according to claim 16, wherein the organic polymeric matrix is a solution based on alginate.
18. The respirometric measurement system according to claim 16, wherein capsules are adjustable on number and/or size and/or contents.
19. The respirometric measurement system according to claim 18, wherein the contents of the capsules are adjustable to the characteristics of the water to be monitored.
20. The respirometric measurement system according to claim 19, wherein the characteristics of the water to be monitored determinates the quality and quantity of organic load.
21. The respirometric measurement system according to claim 20, wherein the water to be monitored comes from Industrial plants, rivers, lakes or canals (RILES).
22. The respirometric measurement system according to claim 16, wherein further the biosensor is disposable.
23. The respirometric measurement system according to claim 16, wherein the quantity of immobilized biomass is previously generated.
24. The respirometric measurement system according to claim 23, wherein the biomass immobilized quantity is stored in cold maintaining the microorganism viability.
25. The respirometric measurement system according to claims 16 to 24, wherein the priming an activating time of the Biosensor is at least 4 hours.
26. The respirometric measurement system according to claims 16 to 25, wherein the priming or activating time of the Biosensor is no longer than 24 hours.
27. Method for fast determining of BOD (Biochemical Oxygen Demand) on water's flow wherein it comprises the following steps: a. provide a removable biosensor with a immobilized biomass quantity on gels capsules that contains bacterias and a organic polymeric matrix; b. provide a removable dissolved oxygen sensor inside the biosensor; c. injecting a water sample to be monitored into the interior of the biosensor; d. register the values of dissolved oxygen that comes of the sensor of step b); e. processing obtained data of the step d); and f. obtain BOD values compared with known measurements OfBOD5.
28. The method according to claim 27, wherein further comprises previous generation of the quantity of immobilized biomass on capsules.
29. The method according to claim 28, wherein further comprises cold storage of the quantity of biomass previously generated.
30. The method according to claim 27, wherein further comprises prime or activate the biosensor.
31. The method according to claim 30, wherein the activating time of the biosensor is at least 4 hours.
32. The method according to claim 31, wherein the activating time of the biosensor is no longer than 24 hours.
33. The method according to claim 27, wherein the step of injecting a water sample is done injecting the entire sample at a time.
34. The method according to claim 27, wherein the organic polymeric matrix is an alginate based solution.
35. The method according to claim 27, wherein capsules are adjustable on number and/or size and/or content.
36. The method according to claim 35, wherein the capsules contents are adjustable to the characteristics of water to be monitored.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/814,000 US20080199902A1 (en) | 2005-01-17 | 2006-01-17 | Biosensor For Determining The Biochemical Oxygen Demand (Bod) By Respirometry |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CL2005000084 | 2005-01-17 | ||
CL84-2005 | 2005-01-17 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2006075030A2 true WO2006075030A2 (en) | 2006-07-20 |
WO2006075030A3 WO2006075030A3 (en) | 2006-08-31 |
Family
ID=36589253
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2006/050235 WO2006075030A2 (en) | 2005-01-17 | 2006-01-17 | Biosensor for determining the biochemical oxygen demand (bod) by respirometry |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2006075030A2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120156711A1 (en) * | 2007-09-18 | 2012-06-21 | Universidad Tecnica Federico Santa Maria | System and method that allows the joined performance of optoelectric and respirometric sensors for instant and accurate ascertainment of biochemical oxygen demand (BOD) in liquid industrial wastes |
US8252582B2 (en) * | 2006-05-11 | 2012-08-28 | Sartorius Stedim Biotech Gmbh | Disposable bioreactor comprising a sensor arrangement |
CN106635931A (en) * | 2017-02-17 | 2017-05-10 | 青岛中科煜成安全技术有限公司 | Engineering bacterium for biochemical oxygen demand (BOD) biosensor |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5385741A (en) * | 1991-02-25 | 1995-01-31 | Champagne Moet & Chandon | Calcium alginate gel partially deficient in calcium ions for use in binding metal cations |
WO2002018563A1 (en) * | 2000-08-31 | 2002-03-07 | Council Of Scientific And Industrial Research | Method for the preparation of stable and reusable biosensing granules |
US20020054828A1 (en) * | 2000-05-31 | 2002-05-09 | Keeping Sean Crispian | Analysis device |
GB2386124A (en) * | 1998-06-20 | 2003-09-10 | Council Scient Ind Res | Process for the preparation of reusable immobilised microbial composition in bead form used as ready-to-use seed inoculum in BOD anaysis of waste water |
-
2006
- 2006-01-17 WO PCT/EP2006/050235 patent/WO2006075030A2/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5385741A (en) * | 1991-02-25 | 1995-01-31 | Champagne Moet & Chandon | Calcium alginate gel partially deficient in calcium ions for use in binding metal cations |
GB2386124A (en) * | 1998-06-20 | 2003-09-10 | Council Scient Ind Res | Process for the preparation of reusable immobilised microbial composition in bead form used as ready-to-use seed inoculum in BOD anaysis of waste water |
US20020054828A1 (en) * | 2000-05-31 | 2002-05-09 | Keeping Sean Crispian | Analysis device |
WO2002018563A1 (en) * | 2000-08-31 | 2002-03-07 | Council Of Scientific And Industrial Research | Method for the preparation of stable and reusable biosensing granules |
Non-Patent Citations (1)
Title |
---|
DATABASE BIOSIS [Online] BIOSCIENCES INFORMATION SERVICE, PHILADELPHIA, PA, US; 1986, SU Y-C ET AL: "A NEW BIOSENSOR FOR RAPID BIOCHEMICAL OXYGEN DEMAND ESTIMATION BY USING IMMOBILIZED GROWING CELL BEADS" XP002388041 Database accession no. PREV198682081943 & PROCEEDINGS OF THE NATIONAL SCIENCE COUNCIL REPUBLIC OF CHINA PART B LIFE SCIENCES, vol. 10, no. 2, 1986, pages 105-112, ISSN: 0255-6596 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8252582B2 (en) * | 2006-05-11 | 2012-08-28 | Sartorius Stedim Biotech Gmbh | Disposable bioreactor comprising a sensor arrangement |
US20120156711A1 (en) * | 2007-09-18 | 2012-06-21 | Universidad Tecnica Federico Santa Maria | System and method that allows the joined performance of optoelectric and respirometric sensors for instant and accurate ascertainment of biochemical oxygen demand (BOD) in liquid industrial wastes |
CN106635931A (en) * | 2017-02-17 | 2017-05-10 | 青岛中科煜成安全技术有限公司 | Engineering bacterium for biochemical oxygen demand (BOD) biosensor |
Also Published As
Publication number | Publication date |
---|---|
WO2006075030A3 (en) | 2006-08-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Horn et al. | Transport of oxygen, sodium chloride, and sodium nitrate in biofilms | |
Gernaey et al. | Activated sludge monitoring with combined respirometric–titrimetric measurements | |
Mathieu et al. | Estimation of wastewater biodegradable COD fractions by combining respirometric experiments in various So/Xo ratios | |
CN101315347B (en) | Device and method for on-line measuring biochemical oxygen demand in sample | |
Wang et al. | An innovative reactor-type biosensor for BOD rapid measurement | |
Quek et al. | Microbial fuel cell biosensor for rapid assessment of assimilable organic carbon under marine conditions | |
Chiu et al. | Oxygen diffusion and consumption in active aerobic granules of heterogeneous structure | |
US5882932A (en) | Continuous quick measurement of biochemical oxygen demand and apparatus | |
EP1996520B1 (en) | A bacterium consortium, bio-electrochemical device and a process for quick and rapid estimation of biological oxygen demand | |
Chiu et al. | Diffusivity of oxygen in aerobic granules | |
US4329232A (en) | Method for measuring biomass viability | |
Li et al. | Effects of pre-conditioning and microbial composition on the sensing efficacy of a BOD biosensor | |
Ramirez-Vargas et al. | Characterization of oxygen transfer in a 24-well microbioreactor system and potential respirometric applications | |
Chiu et al. | Oxygen diffusion in active layer of aerobic granule with step change in surrounding oxygen levels | |
CN102288653A (en) | Online biochemical oxygen demand (BOD) detector and detection method of same | |
CN110186970A (en) | A kind of sewage treatment plant inflow toxicity on-line measuring device | |
Hussain et al. | Real-time biomonitoring of oxygen uptake rate and biochemical oxygen demand using a novel optical biogas respirometric system | |
CN102109512A (en) | Device and method for detecting water toxicity | |
WO2006075030A2 (en) | Biosensor for determining the biochemical oxygen demand (bod) by respirometry | |
JP3664888B2 (en) | BOD biosensor measuring device | |
CN202083662U (en) | Online tester for biochemical oxygen demand BOD | |
CN201935910U (en) | Water quality toxicity detecting device | |
US20080199902A1 (en) | Biosensor For Determining The Biochemical Oxygen Demand (Bod) By Respirometry | |
Rahman et al. | A simple cost-effective manometric respirometer: design and application in wastewater biomonitoring | |
JP5709038B2 (en) | BOD sensor, BOD measuring method and BOD measuring device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DPE1 | Request for preliminary examination filed after expiration of 19th month from priority date (pct application filed from 20040101) | ||
NENP | Non-entry into the national phase in: |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 11814000 Country of ref document: US |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 06707731 Country of ref document: EP Kind code of ref document: A2 |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 6707731 Country of ref document: EP |