CN108102897A - A kind of photosynthetic microorganism hydrogen manufacturing bactogen - Google Patents
A kind of photosynthetic microorganism hydrogen manufacturing bactogen Download PDFInfo
- Publication number
- CN108102897A CN108102897A CN201711246555.4A CN201711246555A CN108102897A CN 108102897 A CN108102897 A CN 108102897A CN 201711246555 A CN201711246555 A CN 201711246555A CN 108102897 A CN108102897 A CN 108102897A
- Authority
- CN
- China
- Prior art keywords
- tank body
- hydrogen
- raw material
- acid
- reaction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- 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
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
-
- 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
- C12M31/00—Means for providing, directing, scattering or concentrating light
- C12M31/02—Means for providing, directing, scattering or concentrating light located outside the reactor
-
- 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
- C12M37/00—Means for sterilizing, maintaining sterile conditions or avoiding chemical or biological contamination
- C12M37/04—Seals
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
-
- 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
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
Abstract
The present invention relates to a kind of photosynthetic microorganism hydrogen manufacturing bactogen, microorganism belonging to genus hydrogen producing technology fields.The present invention adds in the raw material of hydrogen manufacturing in tank body by feed inlet, end cap and tank body are sealed by sealing device, open light emitting source, the in vivo raw material of tank starts to react under light source, a part of raw material in device is pumped by heating unit by high-pressure pump, tank body is again introduced by drainage pipeline after heating, when raw material reacts, pass through temperature sensor, acid-base value detector and pressure gauge etc. detect the extent of reaction of tank interior raw material, it can be reconciled if acid-base value is not up to standard by soda acid attemperation apparatus and ensure acid-base value needed for reaction, the hydrogen generated after reaction is discharged by Hydrogen Line, and waste material is then discharged by waste material discharge line.By the way of being heated in the present invention using outside, ensure the uniform of tank body temperature, make raw material reaction consistent, improve hydrogen production efficiency.
Description
Technical field
The present invention relates to a kind of photosynthetic microorganism hydrogen manufacturing bactogen, microorganism belonging to genus hydrogen producing technology fields.
Background technology
21 century, the whole world is faced with the dual-pressure of economic growth and environmental protection, thus changes the production of the energy
And consumption pattern, it for establishing the energy resource structure of sustainable development, promotes economic development and Improvement of Ecological Environment, all with great
Meaning.Therefore, how rationally to utilize and develop regenerative resource have become countries in the world all must face and solve it is great
Problem.
Regenerative resource generally comprises nuclear energy, solar energy, wind energy, biological intelligence, ocean energy, geothermal energy and Hydrogen Energy etc..It can
The advantages of renewable sources of energy is to gather materials on the spot, safely cleaning, can regenerate, and is directly utilized.Shortcoming is that energy density is low, randomness
The shortcomings of big.In many regenerative resources.Hydrogen is had attracted much attention with superior combustibility and environmental benefit.
Traditional hydrogen production process is because substantial amounts of non-renewable energy resources need to be consumed, thus be not suitable with social sustainable development
Demand.Biomass hydrogen preparation technology has caused extensive in the world as a kind of technology for meeting the strategy of sustainable development
Pay attention to.U.S., moral, Deng states are in depth researched and developed with regard to this technology.What these countries had also specially set up grinds
Study carefully mechanism, while formulate detailed biomass hydrogen preparation development plan.
Biological hydrogen production problem most proposed that the energy crisis of the 1970s causes people to biological hydrogen production earlier than 1966
The extensive concern of technology, the nineties is because of the further understanding to greenhouse effects, the energy of the biological hydrogen production as sustainable development
It draws attention again.Bio-hydrogen production technology is that nature is stored in organic compound（Such as carbohydrate, the albumen in plant
Matter etc.）In energy by the effect of highly effective hydrogen yield bacterium, be converted into hydrogen.Biological hydrogen production was metabolized using certain micro-organisms
One biotechnology of Cheng Laisheng hydrogen producings.It can be organic wastewater, municipal refuse or biomass that its is raw materials used, come
Source is enriched, cheap.Its production process cleans, is energy saving, and does not consume mineral resources.
Biological hydrogen production can substantially be divided into three classes：The water photodissociation production hydrogen of Eukaryotic Algae and cyanobacteria；The light fermentation of photosynthetic bacteria
Produce hydrogen；Dark fermentation and hydrogen production of anaerobic fermentation bacterium etc..
Photosynthetic organism hydrogen generation reactor is the core component of photosynthetic organism hydrogen generation system, although bioreactor
Research and development is very fast, but the starting stage is still within compared with microorganism reactor and fermentation industry, and especially application study relates to
And face is narrow, is only limitted to a few algae.Generally, whether being directly exposed in air according to culture solution and by reactor
It is divided into two kinds of Race-way photobioreactor and sealed bioreactor.
The present invention develops the bactogen of a set of suitable photosynthetic microorganism hydrogen-manufacturing reactor, for photosynthetic microorganism
The propulsion of industries process has certain practical significance.
The content of the invention
Present invention mainly solves the technical issues of：For biohydrogen device hydrogen generation efficiency is low and hydrogen-manufacturing reactor excessively
The problem of complexity is unfavorable for improving bacterial strain hydrogen discharging rate, the present invention provides a kind of photosynthetic microorganism hydrogen manufacturing bactogens.
In order to solve the above-mentioned technical problem, the technical solution adopted in the present invention：
A kind of photosynthetic microorganism hydrogen manufacturing bactogen, including end cap and tank body, be provided on the end cap Hydrogen Line,
Temperature sensor, acid-base value detector and pressure gauge are additionally provided with soda acid attemperation apparatus and pumping conduit on end cap, draw water
Pipeline is connected with heating unit, high-pressure pump is provided in pipeline, heating unit is connected by drainage pipeline with tank body, described
Tank body on the left of be provided with feed inlet, bottom is provided with waste material discharge line, and tank body periphery is provided with light emitting source, tank body and end cap
It is connected by sealing device.
A kind of application process of photosynthetic microorganism hydrogen manufacturing bactogen is：The raw material of hydrogen manufacturing are added by feed inlet
Enter in tank body, seal end cap and tank body by sealing device, open light emitting source, the in vivo raw material of tank starts instead under light source
Should, a part of raw material in device is pumped by heating unit by high-pressure pump, tank body is again introduced by drainage pipeline after heating,
When raw material reacts, the extent of reaction of tank interior raw material is detected by temperature sensor, acid-base value detector and pressure gauge etc.,
It can be reconciled if acid-base value is not up to standard by soda acid attemperation apparatus and ensure acid-base value needed for reaction, the hydrogen generated after reaction leads to
Hydrogen Line discharge is crossed, and waste material is then discharged by waste material discharge line.
The tank body and end cap is all made of transparent material.
The tank body uses double-layer structure, and centre is insulating layer.
The beneficial effects of the invention are as follows：
Reacting tank body is made using transparent material in the present invention, and reacting tank body is barreled, increases the light transmittance of tank body, makes tank
The reaction raw materials in internal portion obtain sufficient light source and carry out photosynthesis, and the present invention is provided with multiple sensors, bag on end cap
Include temperature sensor, acid-base value detector and pressure gauge, by these sensors can detect in real time tank interior temperature,
Pressure and acid-base value, it is ensured that the stability of hydrogen production process uses in of the invention reaction solution extraction heating being pumped into reaction again
The mode of container come ensure reaction temperature, make to be distributed heat to avoid when directly heating in tank body in this way
It is uneven, it is higher in heating unit ambient temperature, and the local temperature from heating unit farther out is relatively low, causes raw material in each portion
Having various reactions for position causes reduction hydrogen production efficiency, in the present invention by the way of the heating of outside, ensures the uniform of tank body temperature, makes
Raw material reaction is consistent, improves hydrogen production efficiency, is provided with light emitting source in the present invention, when being reacted, extraneous sunlight is not
Continual, thus in the present invention be provided with light source, it is ensured that device can Uniformly stable operation, improve hydrogen production efficiency.
Description of the drawings
Fig. 1 is the organigram of photosynthetic microorganism hydrogen manufacturing bactogen of the present invention.
Wherein, 1, Hydrogen Line；2nd, temperature sensor；3rd, sealing device；4th, light emitting source；5th, tank body；6th, waste material discharge pipe
Road；7th, soda acid attemperation apparatus；8th, acid-base value detector；9th, pressure gauge；10th, high-pressure pump；11st, pumping conduit；12nd, heating unit；
13rd, drainage pipeline；14th, feed inlet；15th, end cap.
Specific embodiment
A kind of photosynthetic microorganism hydrogen manufacturing bactogen including end cap 15 and tank body 5, is provided on the end cap 15
Hydrogen Line 1, temperature sensor 2, acid-base value detector 8 and pressure gauge 9 are additionally provided with soda acid attemperation apparatus 7 on end cap 15
And pumping conduit 11, pumping conduit 11 are connected with heating unit 12, and high-pressure pump 10 is provided in pipeline, heating unit 12 is logical
It crosses drainage pipeline 13 with tank body 5 to be connected, 5 left side of tank body is provided with feed inlet 14, and bottom is provided with waste material discharge pipe
Road 6,5 periphery of tank body are provided with light emitting source 4, and tank body 5 is connected with end cap 15 by sealing device 3.A kind of photosynthetic microorganism system
The application process of hydrogen bactogen is：The raw material of hydrogen manufacturing are added in by feed inlet 14 in tank body 5, pass through sealing device
3 seal end cap 15 and tank body 5, opening light emitting source 4, and the raw material in tank body 5 starts to react under light source, will by high-pressure pump 10
A part of raw material is pumped into heating unit 12 in device, and tank body 5 is again introduced by drainage pipeline 13 after heating, is reacted in raw material
When, by the extent of reaction of the detection 5 inside raw material of tank body such as temperature sensor 2, acid-base value detector 8 and pressure gauge 9, if sour
Not up to standard can then be reconciled by soda acid attemperation apparatus 7 of basicity ensures acid-base value needed for reaction, and the hydrogen generated after reaction passes through
Hydrogen Line 1 is discharged, and waste material is then discharged by waste material discharge line 6.The tank body 5 and end cap 15 all use transparent material
It is made.The tank body 5 uses double-layer structure, and centre is insulating layer.
Claims (4)
1. a kind of photosynthetic microorganism hydrogen manufacturing bactogen, including end cap（15）And tank body（5）, the end cap（15）On set
It is equipped with Hydrogen Line（1）, temperature sensor（2）, acid-base value detector（8）And pressure gauge（9）, end cap（15）On be additionally provided with
Soda acid attemperation apparatus（7）And pumping conduit（11）, pumping conduit（11）With heating unit（12）It is connected, is provided in pipeline
High-pressure pump（10）, heating unit（12）Pass through drainage pipeline（13）With tank body（5）It is connected, the tank body（5）Left side is set
There is feed inlet（14）, bottom is provided with waste material discharge line（6）, tank body（5）Periphery is provided with light emitting source（4）, tank body（5）With end
Lid（15）Pass through sealing device（3）It is connected.
2. a kind of application process of photosynthetic microorganism hydrogen manufacturing bactogen according to claim 1 is：By hydrogen manufacturing
Raw material pass through feed inlet（14）Add in tank body（5）In, pass through sealing device（3）Make end cap（15）And tank body（5）Sealing is opened
Light emitting source（4）, tank body（5）Interior raw material starts to react under light source, passes through high-pressure pump（10）By a part of raw material pump in device
Enter heating unit（12）, pass through drainage pipeline after heating（13）It is again introduced into tank body（5）, when raw material reacts, passed by temperature
Sensor（2）, acid-base value detector（8）And pressure gauge（9）Deng detection tank body（5）The extent of reaction of internal raw material, if acid-base value
It is not up to standard then to pass through soda acid attemperation apparatus（7）It reconciles and ensures acid-base value needed for reaction, the hydrogen generated after reaction passes through hydrogen
Feed channel（1）Discharge, and waste material then passes through waste material discharge line（6）Discharge.
3. a kind of photosynthetic microorganism hydrogen manufacturing bactogen according to claim 1, it is characterised in that：The tank body
（5）And end cap（15）All it is made of transparent material.
4. a kind of photosynthetic microorganism hydrogen manufacturing bactogen according to claim 1, it is characterised in that：The tank body
（5）Using double-layer structure, centre is insulating layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711246555.4A CN108102897A (en) | 2017-12-01 | 2017-12-01 | A kind of photosynthetic microorganism hydrogen manufacturing bactogen |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711246555.4A CN108102897A (en) | 2017-12-01 | 2017-12-01 | A kind of photosynthetic microorganism hydrogen manufacturing bactogen |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108102897A true CN108102897A (en) | 2018-06-01 |
Family
ID=62207963
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711246555.4A Pending CN108102897A (en) | 2017-12-01 | 2017-12-01 | A kind of photosynthetic microorganism hydrogen manufacturing bactogen |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108102897A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112266848A (en) * | 2020-11-09 | 2021-01-26 | 河南农业大学 | Novel no pump formula inner loop formula photosynthetic biological hydrogen production reactor |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2918431Y (en) * | 2006-06-12 | 2007-07-04 | 河南农业大学 | Photosynthetic microorganism hydrogen production reactor |
| CN101974409A (en) * | 2010-11-27 | 2011-02-16 | 福州大北农生物技术有限公司 | Bacterial culture fermentation tank device and fermentation technology thereof |
| CN203904331U (en) * | 2014-05-12 | 2014-10-29 | 上海海洋大学 | Intensive-mode microalgae photobioreactor device |
| CN205954015U (en) * | 2016-07-07 | 2017-02-15 | 郑州新农源绿色食品有限公司 | Beans clear water fermenting installation |
| CN206157155U (en) * | 2016-10-26 | 2017-05-10 | 云南农业职业技术学院 | Anaerobic fermentation device |
-
2017
- 2017-12-01 CN CN201711246555.4A patent/CN108102897A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2918431Y (en) * | 2006-06-12 | 2007-07-04 | 河南农业大学 | Photosynthetic microorganism hydrogen production reactor |
| CN101974409A (en) * | 2010-11-27 | 2011-02-16 | 福州大北农生物技术有限公司 | Bacterial culture fermentation tank device and fermentation technology thereof |
| CN203904331U (en) * | 2014-05-12 | 2014-10-29 | 上海海洋大学 | Intensive-mode microalgae photobioreactor device |
| CN205954015U (en) * | 2016-07-07 | 2017-02-15 | 郑州新农源绿色食品有限公司 | Beans clear water fermenting installation |
| CN206157155U (en) * | 2016-10-26 | 2017-05-10 | 云南农业职业技术学院 | Anaerobic fermentation device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112266848A (en) * | 2020-11-09 | 2021-01-26 | 河南农业大学 | Novel no pump formula inner loop formula photosynthetic biological hydrogen production reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Das et al. | Molecular biohydrogen production by dark and photo fermentation from wastes containing starch: recent advancement and future perspective | |
| Lo et al. | Sequential dark–photo fermentation and autotrophic microalgal growth for high-yield and CO2-free biohydrogen production | |
| Lin et al. | Fermentative hydrogen production from wastewaters: a review and prognosis | |
| CN201686627U (en) | Fermentation device for treating organic wastes | |
| CN201670835U (en) | Garage type anaerobic dry fermentation device | |
| CN100357174C (en) | Heat treatment-fermented hy drogen-generating method by preparing hydrogen from residual sludge for sewage treatment plant | |
| CN103146568B (en) | Dark-l fermentation integrated biological hydrogen production device | |
| CN107012089A (en) | Batch-type synchronous saccharification photosynthetic organism hydrogen generation reactor and its hydrogen manufacturing operating method | |
| Kumar et al. | Improved hydrogen production from galactose via immobilized mixed consortia | |
| CN101063098B (en) | Culture method for photosynthetic bacterium strain having hydrogen-generation specificity | |
| CN105154313B (en) | A kind of dark fermentation photosynthesis joint hydrogen production bioreactor and its production hydrogen methods | |
| CN108102897A (en) | A kind of photosynthetic microorganism hydrogen manufacturing bactogen | |
| CN103993041B (en) | A kind of method that utilization microalgae improves hydrogen output | |
| Almomani et al. | Application of microalgae in wastewater treatment: simultaneous nutrient removal and carbon dioxide bio-fixation for biofuel feedstock production | |
| CN105039416A (en) | Method for improving fermentation efficiency of anaerobic qi-eating microorganisms | |
| CN101275117B (en) | Method for fast algae proliferation directly used for bio-hydrogen production by using CO2 | |
| CN100352911C (en) | High performance solar methane generator | |
| CN102363794A (en) | Method for producing hydrogen through kitchen waste enzymolysis and reinforced dark fermentation | |
| CN204369742U (en) | A kind of anaerobic sludge digestion and marsh gas purifying synchronization processing apparatus | |
| CN101280273A (en) | Industrialized culture method and device for photosynthetic autotroph | |
| CN101413014A (en) | Method and apparatuses for pretreating sewage plant excess sludge by microwave method and producing hydrogen by fermentation | |
| CN105624026A (en) | Low-carbon zero-emission circulating hydrogen preparing device | |
| CN101974411B (en) | Organic household garbage hydrogen production device | |
| CN114226394A (en) | Medium-temperature aerobic bioreactor applied to refuse landfill | |
| CN103725606B (en) | Use method of sequencing batch type biological hydrogen production reactor |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180601 |