USH831H - Tubular biofilm reactor - Google Patents
Tubular biofilm reactor Download PDFInfo
- Publication number
- USH831H USH831H US07/039,851 US3985187A USH831H US H831 H USH831 H US H831H US 3985187 A US3985187 A US 3985187A US H831 H USH831 H US H831H
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- United States
- Prior art keywords
- biofilm
- sampler
- tubular
- continuous flow
- flow stream
- 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.)
- Abandoned
Links
- 244000005700 microbiome Species 0.000 claims abstract description 7
- 238000012544 monitoring process Methods 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 7
- 238000007689 inspection Methods 0.000 abstract description 2
- 239000003139 biocide Substances 0.000 description 7
- 239000012530 fluid Substances 0.000 description 7
- 241000894006 Bacteria Species 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000003115 biocidal effect Effects 0.000 description 4
- 230000001464 adherent effect Effects 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 230000003134 recirculating effect Effects 0.000 description 2
- 238000005070 sampling Methods 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 208000034699 Vitreous floaters Diseases 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000004599 antimicrobial Substances 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000032770 biofilm formation Effects 0.000 description 1
- 239000006285 cell suspension Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 235000021232 nutrient availability Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000010349 pulsation Effects 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Q—MEASURING OR TESTING PROCESSES INVOLVING ENZYMES, NUCLEIC ACIDS OR MICROORGANISMS; COMPOSITIONS OR TEST PAPERS THEREFOR; PROCESSES OF PREPARING SUCH COMPOSITIONS; CONDITION-RESPONSIVE CONTROL IN MICROBIOLOGICAL OR ENZYMOLOGICAL PROCESSES
- C12Q1/00—Measuring or testing processes involving enzymes, nucleic acids or microorganisms; Compositions therefor; Processes of preparing such compositions
- C12Q1/02—Measuring or testing processes involving enzymes, nucleic acids or microorganisms; Compositions therefor; Processes of preparing such compositions involving viable microorganisms
- C12Q1/025—Measuring or testing processes involving enzymes, nucleic acids or microorganisms; Compositions therefor; Processes of preparing such compositions involving viable microorganisms for testing or evaluating the effect of chemical or biological compounds, e.g. drugs, cosmetics
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Q—MEASURING OR TESTING PROCESSES INVOLVING ENZYMES, NUCLEIC ACIDS OR MICROORGANISMS; COMPOSITIONS OR TEST PAPERS THEREFOR; PROCESSES OF PREPARING SUCH COMPOSITIONS; CONDITION-RESPONSIVE CONTROL IN MICROBIOLOGICAL OR ENZYMOLOGICAL PROCESSES
- C12Q1/00—Measuring or testing processes involving enzymes, nucleic acids or microorganisms; Compositions therefor; Processes of preparing such compositions
- C12Q1/02—Measuring or testing processes involving enzymes, nucleic acids or microorganisms; Compositions therefor; Processes of preparing such compositions involving viable microorganisms
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/02—Devices for withdrawing samples
- G01N1/10—Devices for withdrawing samples in the liquid or fluent state
- G01N1/20—Devices for withdrawing samples in the liquid or fluent state for flowing or falling materials
- G01N1/2035—Devices for withdrawing samples in the liquid or fluent state for flowing or falling materials by deviating part of a fluid stream, e.g. by drawing-off or tapping
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N17/00—Investigating resistance of materials to the weather, to corrosion, or to light
- G01N17/008—Monitoring fouling
-
- 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
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N1/00—Sampling; Preparing specimens for investigation
- G01N1/02—Devices for withdrawing samples
- G01N1/04—Devices for withdrawing samples in the solid state, e.g. by cutting
Definitions
- biocides are used to control the growth of microorganisms in flowing or stagnant systems (piping, transit lines, tanks, cooling water and waste water systems) which can become fouled due to biofilm development.
- bacteria are able to adhere to a variety of surfaces (steel, glass, plastic). Bacterial attachment to surfaces is affected by several factors including surface charge and energy, hydrophobicity, nutrient availability, fluid flow and shear, microorganism type and temperature.
- microbes absorb nutrients from the flowing fluid, grow as an adhered biomass and produce extracellular slime.
- the fibrillar network of slime allows the cells to attach to each other and maintain successive populations on the adhering surface.
- the fouling biomass can eventually increase frictional resistance of fluid flow and in severe cases cause plugging of a tubular system.
- biofouled surfaces of metals undergo a progressive deterioration characterized by complex chemical and biochemical oxidation-reduction reactions in which bacteria (e.g. sulfate-reducing bacteria) can initiate or accelerate the corrosion process.
- the primary purpose of the present invention is to provide a method and apparatus for monitoring biofouling by microorganisms in a continuous flow stream, which produce accurate results and which do not interfere with the continuous flow stream being monitored. Accordingly, an apparatus is provided for monitoring biofouling by microorganisms in a continuous flow stream, wherein tubulars connect a series of biofilm samplers and provide bypasses around each sampler, and whereby each sampler is removable for inspection without interruption of the continuous flow stream.
- each sampler has a contoured surface which is in contact with the continuous flow stream and flush with the inner surface of the tubular means.
- the present invention also pertains to a method for monitoring biofouling by microorganisms in a continuous flow stream, including connecting a series of biofilm samplers with tubulars, bypassing the continuous flow stream around at least one of the biofilm samplers, and checking the bypassed biofilm sampler for biofouling.
- the method includes positioning each sampler such that a contoured surface of the sampler is in contact with the continuous flow stream and flush with the inner surface of the tubular means.
- FIG. 1 is a schematic of a high pressure/high flow rate tubular biofilm reactor.
- FIG. 2 shows a biofilm sampler
- FIG. 3 shows a holder for the biofilm sampler.
- FIG. 4 shows a biofilm sampler, such as shown in FIG. 2, inserted into the holder, such as shown in FIG. 3.
- the present invention is a continuous flow tubular device which can be used to screen biocides for biofilm control.
- the present invention differs from the above-discussed Robbins device in that it (a) is constructed of stainless steel and can be used with saline water (e.g.
- (b) can be operated under high pressure (up to about 1500 psi, or greater), and therefore, simulate injection pressures of tubulars entering well-bore zones in a reservoir, (c) can be operated at high flow (up to about 1.5 liters per minute, or greater, through the tubular) of field injection systems, and (d) has a system of shut-off valves for continuous biofilm sampling without interfering with flow through the pressurized tubular.
- the following describes the construction and operation of the present invention which can (1) detect adherent populations of sulfate-reducing bacteria, and aerobic organisms or the like in a flowing tubular system, and (2) be used to determine optimum biocide levels and dosing regimes to control such biofouling.
- FIGS. 1-3 Schematics for the continuous flow tubular system and the biosamplers of the invention are shown in FIGS. 1-3.
- Each four-way fitting 1-5 contains two studs or biosamplers, such as samplers 6 and 7 shown in FIG. 3 which are machined to set flush with the inside of the tubular wall. Biofilm growth occurs on the flush-fitting concave surface 8 shown in FIG. 2.
- the biosamplers are preferably manufactured of carbonless steel or stainless steel. The process of the invention requires connecting at least two biofilm samplers with tubular means.
- the tubular system is equipped with bypasses 9-13 around each pair of biosamplers in each four-way fitting 1-5, for diverting fluid flow. This allows for inspecting the biosamplers while the tubular system is operating continuously under high pressure and flow.
- bypass four-way fitting 1 for example, valves 14 and 15 are closed, and valves 16 and 17 are opened (while valves 18-21 remain closed and valves 22-29 remain open).
- Other combinations of open and closed valves can be utilized to bypass any one, combination or all of the four-way fittings.
- valves 14 and 29 may be closed and valves 16 and 21 opened (while valves 17-20 remain closed) in order to bypass all the four-way fittings.
- Pump 30 supplies fluid for analysis from container 31 which may contain, for example, seawater.
- a flush line 32 is provided to pressure the container, for example with nitrogen.
- a recirculating fluid pump 33 is utilized to provide circulation through the four-way fittings 1-5. Both pumps preferably are rated at pressures of at least about 1500 psi.
- Pressure in the tubular system is supplied from back pressure regulator 34, preferably using deoxygenated nitrogen and a high capacity gas purifier 35 with a bottoms drawoff, e.g. H 2 O-N 2 .
- the tubular reactor is also equipped with a Jorgenson gauge 36 for removing any excess entrained gases.
- a coaxial heat exchanger 37 is used for removing heat generated during the temperature control experiments (with heating fluid, e.g.
- a pulsation dampener 38 is used to reduce large pulse variations from the recirculating pump 33.
- Pressure relief valves 39 and 40 are provided as safety measures for potential pressure increases in the system, along with over pressure relief 41.
- temperature checks 42-44 are used to monitor temperature changes, and a rotameter 15a is provided to check flow rates.
- FIGS. 2 and 3 provide an exploded view of the biofilm sampler and holder.
- the biofilm sampler utilizes an O-ring 44 and a locking ring 45 to hold the sampler in place with lock nuts 46 and 47 in the holder shown in FIG. 3.
- the groove is aligned to properly orient the surface 8 with respect to the inside walls of the tubulars.
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Immunology (AREA)
- Physics & Mathematics (AREA)
- Microbiology (AREA)
- Proteomics, Peptides & Aminoacids (AREA)
- Genetics & Genomics (AREA)
- General Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- Biotechnology (AREA)
- Molecular Biology (AREA)
- Pathology (AREA)
- Biophysics (AREA)
- Medicinal Chemistry (AREA)
- Sustainable Development (AREA)
- Environmental & Geological Engineering (AREA)
- Environmental Sciences (AREA)
- Ecology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Biomedical Technology (AREA)
- Toxicology (AREA)
- Hydrology & Water Resources (AREA)
- Food Science & Technology (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Sampling And Sample Adjustment (AREA)
Abstract
A tubular connected series of biofilm samplers is provided for monitoring biofouling by microorganisms in a continuous flow stream. Tubular bypasses are provided around each sampler, so that each sampler is removable for inspection of biofouling without interruption of the continuous flow stream. In addition, each sampler has a contoured surface which is in contact with the continuous flow stream and which is flush with the inner surface of the tubulars connecting the samplers.
Description
This is a continuation of application Ser. No. 603,016, filed Apr. 23, 1984, now abandoned.
Commercial biocides are used to control the growth of microorganisms in flowing or stagnant systems (piping, transit lines, tanks, cooling water and waste water systems) which can become fouled due to biofilm development. In many flowing aquatic systems, bacteria are able to adhere to a variety of surfaces (steel, glass, plastic). Bacterial attachment to surfaces is affected by several factors including surface charge and energy, hydrophobicity, nutrient availability, fluid flow and shear, microorganism type and temperature. As colonization progresses, microbes absorb nutrients from the flowing fluid, grow as an adhered biomass and produce extracellular slime. The fibrillar network of slime allows the cells to attach to each other and maintain successive populations on the adhering surface. The fouling biomass can eventually increase frictional resistance of fluid flow and in severe cases cause plugging of a tubular system. In addition, biofouled surfaces of metals undergo a progressive deterioration characterized by complex chemical and biochemical oxidation-reduction reactions in which bacteria (e.g. sulfate-reducing bacteria) can initiate or accelerate the corrosion process.
In studies of biofilm formation, McCoy et al (1981, Canad, J. Microbial. 27:910) and Ruseskca et al (1982, Oil and Gas J., March 8, pp 253-264) have described a continuous flow tubular recycle reactor for biofilm sampling (hereinafter referred to as the Robbins device) which can be placed as a bypass or slipstream into an existing flow system. The Robbins device has removable test surfaces (studs) for studying the development of biofilm growth and evaluating biocide effectiveness. The present invention is an improvement over the Robbins device, which suffers from several inadequacies, as will be described more particularly hereinafter.
The primary purpose of the present invention is to provide a method and apparatus for monitoring biofouling by microorganisms in a continuous flow stream, which produce accurate results and which do not interfere with the continuous flow stream being monitored. Accordingly, an apparatus is provided for monitoring biofouling by microorganisms in a continuous flow stream, wherein tubulars connect a series of biofilm samplers and provide bypasses around each sampler, and whereby each sampler is removable for inspection without interruption of the continuous flow stream. Preferably, each sampler has a contoured surface which is in contact with the continuous flow stream and flush with the inner surface of the tubular means.
The present invention also pertains to a method for monitoring biofouling by microorganisms in a continuous flow stream, including connecting a series of biofilm samplers with tubulars, bypassing the continuous flow stream around at least one of the biofilm samplers, and checking the bypassed biofilm sampler for biofouling. Preferably, the method includes positioning each sampler such that a contoured surface of the sampler is in contact with the continuous flow stream and flush with the inner surface of the tubular means.
Other purposes, distinctions over the art, advantages and features of the invention will be apparent to one skilled in the art upon review of the following.
FIG. 1 is a schematic of a high pressure/high flow rate tubular biofilm reactor.
FIG. 2 shows a biofilm sampler.
FIG. 3 shows a holder for the biofilm sampler.
FIG. 4 shows a biofilm sampler, such as shown in FIG. 2, inserted into the holder, such as shown in FIG. 3.
Traditional biocide testing, e.g., in cell suspension (free-floating or planktonic organisms) assays, has been inadequate for inhibiting aerobic and anaerobic organisms that colonize surfaces (sessile or adherent populations). Higher doses of an antimicrobial agent which are active against the free-floaters at lower levels, are required to kill or reduce the sessile organisms accumulating on surfaces. Attached microbes are more refractory to biocide inhibition mainly because these compounds cannot penetrate the biofilm surface with its many layers of cells and exocellular polysaccharide slime.
In oilfield waterflood operations water-borne aerobic organisms and sulfate-reducing bacteria can potentially cause biofouling and corrosion of injection and production tubulars, water treating facilities and transfer lines. It is possible through the prudent field use of biocides to control adherent microbial growth, a substantial savings in yearly replacement cost of corroded and biofouled piping can be obtained. This need in the art has led to the present invention which is a continuous flow tubular device which can be used to screen biocides for biofilm control. The present invention differs from the above-discussed Robbins device in that it (a) is constructed of stainless steel and can be used with saline water (e.g. seawater), (b) can be operated under high pressure (up to about 1500 psi, or greater), and therefore, simulate injection pressures of tubulars entering well-bore zones in a reservoir, (c) can be operated at high flow (up to about 1.5 liters per minute, or greater, through the tubular) of field injection systems, and (d) has a system of shut-off valves for continuous biofilm sampling without interfering with flow through the pressurized tubular.
The following describes the construction and operation of the present invention which can (1) detect adherent populations of sulfate-reducing bacteria, and aerobic organisms or the like in a flowing tubular system, and (2) be used to determine optimum biocide levels and dosing regimes to control such biofouling.
Schematics for the continuous flow tubular system and the biosamplers of the invention are shown in FIGS. 1-3. The entire tubular system, preferably about 1/4-inch inside diameter tubing, and all valves and all four-way fittings are preferably made of stainless steel and have a maximum pressure rating of approximately 5000 psi or greater. Each four-way fitting 1-5 contains two studs or biosamplers, such as samplers 6 and 7 shown in FIG. 3 which are machined to set flush with the inside of the tubular wall. Biofilm growth occurs on the flush-fitting concave surface 8 shown in FIG. 2. The biosamplers are preferably manufactured of carbonless steel or stainless steel. The process of the invention requires connecting at least two biofilm samplers with tubular means. The tubular system is equipped with bypasses 9-13 around each pair of biosamplers in each four-way fitting 1-5, for diverting fluid flow. This allows for inspecting the biosamplers while the tubular system is operating continuously under high pressure and flow. To bypass four-way fitting 1, for example, valves 14 and 15 are closed, and valves 16 and 17 are opened (while valves 18-21 remain closed and valves 22-29 remain open). Other combinations of open and closed valves can be utilized to bypass any one, combination or all of the four-way fittings. For example, valves 14 and 29 may be closed and valves 16 and 21 opened (while valves 17-20 remain closed) in order to bypass all the four-way fittings.
Pump 30 supplies fluid for analysis from container 31 which may contain, for example, seawater. A flush line 32 is provided to pressure the container, for example with nitrogen. A recirculating fluid pump 33 is utilized to provide circulation through the four-way fittings 1-5. Both pumps preferably are rated at pressures of at least about 1500 psi. Pressure in the tubular system is supplied from back pressure regulator 34, preferably using deoxygenated nitrogen and a high capacity gas purifier 35 with a bottoms drawoff, e.g. H2 O-N2. The tubular reactor is also equipped with a Jorgenson gauge 36 for removing any excess entrained gases. A coaxial heat exchanger 37 is used for removing heat generated during the temperature control experiments (with heating fluid, e.g. H2 O, shown going in and out), and a pulsation dampener 38 is used to reduce large pulse variations from the recirculating pump 33. Pressure relief valves 39 and 40 are provided as safety measures for potential pressure increases in the system, along with over pressure relief 41. In addition, temperature checks 42-44 are used to monitor temperature changes, and a rotameter 15a is provided to check flow rates.
FIGS. 2 and 3 provide an exploded view of the biofilm sampler and holder. The biofilm sampler utilizes an O-ring 44 and a locking ring 45 to hold the sampler in place with lock nuts 46 and 47 in the holder shown in FIG. 3. Preferably, when the sampler is secured in place in the four-way fitting, as shown on the right hand side of FIG. 2, the groove is aligned to properly orient the surface 8 with respect to the inside walls of the tubulars.
The foregoing description of the invention is merely intended to be explanatory thereof, and various changes in the details of the described method and apparatus may be made within the scope of the appended claims without departing from the spirit of the invention.
Claims (1)
1. A method for monitoring biofilm microorganisms in a continuous flow stream, comprising (a) connecting biofilm samplers with tubular means, (b) passing a continuous flow stream through the samplers, (c) bypassing the continuous flow stream around at least one biofilm sampler, and (d) checking the one biofilm sampler for biofouling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US07/039,851 USH831H (en) | 1984-04-23 | 1987-04-20 | Tubular biofilm reactor |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US60301684A | 1984-04-23 | 1984-04-23 | |
| US07/039,851 USH831H (en) | 1984-04-23 | 1987-04-20 | Tubular biofilm reactor |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US60301684A Continuation | 1984-04-23 | 1984-04-23 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| USH831H true USH831H (en) | 1990-10-02 |
Family
ID=26716515
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/039,851 Abandoned USH831H (en) | 1984-04-23 | 1987-04-20 | Tubular biofilm reactor |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | USH831H (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1993001497A3 (en) * | 1991-07-11 | 1993-03-18 | Kiwa Nv | Monitor for growth and deposit |
| EP0676233A1 (en) * | 1994-04-09 | 1995-10-11 | STEAG Aktiengesellschaft | Membrane monitoring for reverse osmosis process |
| US20020081727A1 (en) * | 2000-06-28 | 2002-06-27 | Liu Shi V. | Method and apparatus for producing age-synchronized cells |
| ES2222057A1 (en) * | 2001-11-14 | 2005-01-16 | Universitat Politecnica De Catalunya | METHOD AND SYSTEM FOR THE FOLLOW-UP OF THE FORMATION OF BIOFILMS. |
| NL2009745C2 (en) * | 2012-11-02 | 2014-05-06 | Kwr Water B V | Monitor for growth and deposit. |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1510195A (en) | 1919-08-27 | 1924-09-30 | Deutsch Koloniale Gerb & Farbs | Fermentation process |
| US1837858A (en) | 1928-02-17 | 1931-12-22 | Worthington Pump & Mach Corp | Sampler |
| US2484279A (en) | 1945-06-11 | 1949-10-11 | Phillips Petroleum Co | Method and apparatus for testing corrosion |
| US3083577A (en) | 1959-04-13 | 1963-04-02 | Jersey Prod Res Co | Fluid sampler |
| US3591454A (en) | 1968-05-22 | 1971-07-06 | Forschunginstitut Fur Die Gasu | Process and apparatus for the continuous fermentation of draff-containing mashes |
-
1987
- 1987-04-20 US US07/039,851 patent/USH831H/en not_active Abandoned
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1510195A (en) | 1919-08-27 | 1924-09-30 | Deutsch Koloniale Gerb & Farbs | Fermentation process |
| US1837858A (en) | 1928-02-17 | 1931-12-22 | Worthington Pump & Mach Corp | Sampler |
| US2484279A (en) | 1945-06-11 | 1949-10-11 | Phillips Petroleum Co | Method and apparatus for testing corrosion |
| US3083577A (en) | 1959-04-13 | 1963-04-02 | Jersey Prod Res Co | Fluid sampler |
| US3591454A (en) | 1968-05-22 | 1971-07-06 | Forschunginstitut Fur Die Gasu | Process and apparatus for the continuous fermentation of draff-containing mashes |
Non-Patent Citations (3)
| Title |
|---|
| "Biocide Testing Against Corrosion-Causing Oil-Field Bacteria Helps Control Plugging", article from Oil & Gas Journal, Mar. 8, 1982, pp. 253-264. |
| "Observations of Fouling Biofilm Formation", W. F. McCoy, et al, 1981 National Research Council of Canada, pp. 910-917. |
| Brochure from Microbios Ltd., Calgary, Alberta, Canada, re "The Robbins Biofilm Sampler". |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1993001497A3 (en) * | 1991-07-11 | 1993-03-18 | Kiwa Nv | Monitor for growth and deposit |
| EP0676233A1 (en) * | 1994-04-09 | 1995-10-11 | STEAG Aktiengesellschaft | Membrane monitoring for reverse osmosis process |
| US20020081727A1 (en) * | 2000-06-28 | 2002-06-27 | Liu Shi V. | Method and apparatus for producing age-synchronized cells |
| US6767734B2 (en) * | 2000-06-28 | 2004-07-27 | Shi Liu | Method and apparatus for producing age-synchronized cells |
| ES2222057A1 (en) * | 2001-11-14 | 2005-01-16 | Universitat Politecnica De Catalunya | METHOD AND SYSTEM FOR THE FOLLOW-UP OF THE FORMATION OF BIOFILMS. |
| NL2009745C2 (en) * | 2012-11-02 | 2014-05-06 | Kwr Water B V | Monitor for growth and deposit. |
| EP2728351A1 (en) * | 2012-11-02 | 2014-05-07 | KWR Water B.V. | Method and apparatus for monitoring the formation of deposits |
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