CN108083227A - A kind of new volatile organic compounds control device - Google Patents
A kind of new volatile organic compounds control device Download PDFInfo
- Publication number
- CN108083227A CN108083227A CN201810130825.3A CN201810130825A CN108083227A CN 108083227 A CN108083227 A CN 108083227A CN 201810130825 A CN201810130825 A CN 201810130825A CN 108083227 A CN108083227 A CN 108083227A
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- Prior art keywords
- chamber
- matrix
- evenly
- favourable turn
- union
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- 239000012855 volatile organic compound Substances 0.000 title claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 61
- 230000005611 electricity Effects 0.000 claims abstract description 45
- 230000002349 favourable effect Effects 0.000 claims abstract description 43
- 239000011159 matrix material Substances 0.000 claims description 40
- 238000005086 pumping Methods 0.000 claims description 27
- 238000005485 electric heating Methods 0.000 claims description 19
- 238000010438 heat treatment Methods 0.000 claims description 12
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 10
- 229910052748 manganese Inorganic materials 0.000 claims description 10
- 239000011572 manganese Substances 0.000 claims description 10
- 230000035939 shock Effects 0.000 claims description 10
- 229940123973 Oxygen scavenger Drugs 0.000 claims description 6
- 238000007599 discharging Methods 0.000 claims description 6
- 230000037452 priming Effects 0.000 claims description 6
- 239000001257 hydrogen Substances 0.000 description 33
- 229910052739 hydrogen Inorganic materials 0.000 description 33
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 32
- 239000007789 gas Substances 0.000 description 31
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 25
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 18
- 229960004424 carbon dioxide Drugs 0.000 description 17
- 229910002092 carbon dioxide Inorganic materials 0.000 description 15
- 239000001569 carbon dioxide Substances 0.000 description 15
- 238000000855 fermentation Methods 0.000 description 13
- 230000004151 fermentation Effects 0.000 description 13
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 9
- 229910002091 carbon monoxide Inorganic materials 0.000 description 9
- 239000004615 ingredient Substances 0.000 description 9
- 150000002431 hydrogen Chemical class 0.000 description 8
- 239000000243 solution Substances 0.000 description 7
- 239000002699 waste material Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000010025 steaming Methods 0.000 description 3
- -1 vapor Chemical compound 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910002090 carbon oxide Inorganic materials 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/48—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents followed by reaction of water vapour with carbon monoxide
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
- C01B3/52—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification by contacting with liquids; Regeneration of used liquids
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F11/00—Other organic fertilisers
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- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
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- 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
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- 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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0205—Processes for making hydrogen or synthesis gas containing a reforming step
- C01B2203/0227—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step
- C01B2203/0233—Processes for making hydrogen or synthesis gas containing a reforming step containing a catalytic reforming step the reforming step being a steam reforming step
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- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/02—Processes for making hydrogen or synthesis gas
- C01B2203/0283—Processes for making hydrogen or synthesis gas containing a CO-shift step, i.e. a water gas shift step
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- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/0475—Composition of the impurity the impurity being carbon dioxide
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- C01B2203/10—Catalysts for performing the hydrogen forming reactions
- C01B2203/1041—Composition of the catalyst
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- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/12—Feeding the process for making hydrogen or synthesis gas
- C01B2203/1205—Composition of the feed
- C01B2203/1211—Organic compounds or organic mixtures used in the process for making hydrogen or synthesis gas
- C01B2203/1235—Hydrocarbons
- C01B2203/1241—Natural gas or methane
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
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- General Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Biomedical Technology (AREA)
- Sustainable Development (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention discloses a kind of new volatile organic compounds control devices,Including stirring evenly device,It is arranged at first reaction unit stirred evenly on the right side of device,The second reaction unit being arranged on the right side of first reaction unit and the collection device being arranged on the right side of second reaction unit,The device that stirs evenly includes tank shell,Tank shell four angles bottom is equipped with idler wheel equipped with hornblock and each hornblock bottom simultaneously,It is provided in the tank shell and stirs evenly chamber,Described stir evenly is fixedly installed the first assembling stand on the downside of chamber at the center of inner wall,The first electricity favourable turn is fixedly installed in first assembling stand,The first electricity favourable turn upper end stirs evenly arm by steering spindle power connector,The described arm lower face or so that stirs evenly mutually claims and is fixedly installed to stir evenly axis,It is stirred evenly described in connection and is provided with cover net between the steering spindle of arm and the first electricity favourable turn and first assembling stand.
Description
Technical field
The present invention relates to organic compound technical fields, are specifically a kind of new volatile organic compounds control device.
Background technology
China is large agricultural country, and agricultural planting area is extremely wide, and more organic agricultural straw can be left after agriculture harvest
Stalk, these stalks be not also easy to produce escaping gas after dealing carefully with, and extremely serious destruction, many institute's weeks are caused to environment
Know that some organic stalks can generate biogas after fermentation, and biogas can be made into hydrogen after reaction treatment, and hydrogen is great ring
Therefore the novel energy of guarantor's type, should provide a kind of organic compound control device for being capable of fast hydrogen making to realize the utilization of resources
Change.
The content of the invention
The technical problems to be solved by the invention are to provide a kind of new volatile organic compounds control device, can
Solve the problems, such as above-mentioned show in the art.
The present invention is achieved through the following technical solutions：A kind of new volatile organic compounds control of the present invention
Device, including stirring evenly device, being arranged at first reaction unit stirred evenly on the right side of device, be arranged at first reaction unit
Second reaction unit on right side and the collection device being arranged on the right side of second reaction unit, the device that stirs evenly include case
Housing, tank shell four angles bottom are equipped with idler wheel, the tank shell equipped with hornblock and each hornblock bottom simultaneously
It is inside provided with and stirs evenly chamber, described stir evenly is fixedly installed the first assembling stand, first assembling stand on the downside of chamber at the center of inner wall
The first electricity favourable turn is inside fixedly installed, the first electricity favourable turn outside is equipped with shield and carries device, and the shield, which carries device, includes shock absorbing block
With except hot fin, the first electricity favourable turn upper end stirs evenly arm by steering spindle power connector, it is described that stir evenly arm lower face or so mutual
Claim and be fixedly installed to stir evenly axis, the steering spindle and the described first assembling of arm and the described first electricity favourable turn are stirred evenly described in connection
Be provided with cover net between seat, it is described stir evenly chamber and get close in the inner left wall of downside inner wall be provided with and the row for stirring evenly chamber unicom
Go out slot, the discharge slot left end is provided with the first cover, it is described stir evenly chamber and get close in the inner left wall of upper inside walls be fixedly installed
There is the second assembling stand, cavity is provided on second assembling stand, it is fixed between the cavity upper inside walls and downside inner wall to set
Be equipped with oxygen scavenger, it is described stir evenly chamber and get close to feeding groove is provided in the upper inside walls of inner left wall, be provided on the feeding groove
Second cover mutually claims before and after the second cover upper surface to be provided with handle.
As preferred technical solution, first reaction unit includes being arranged at first base stirred evenly on the right side of device
Body is provided with the first accommodating chamber in first matrix, is provided in the first accommodating chamber inner left wall and described first holds
It receives and the first of chamber unicom connects union, described first, which connects union left end, is connected to the tank shell upper surface and stirs evenly chamber connection with described
Logical, described first connects the first pumping device is provided in union, and described first, which connects unicom in union, is provided with steam pipe, the steaming
It is provided with open and close valve on steam pipe, described first connects the first intake valve is provided in union, solid in the inner wall of first accommodating chamber
Surely the manganese block of annular is provided with, first matrix outer is provided with the first electric hot plate of annular, is set in first electric hot plate
The first electric heating chamber of annular is equipped with, the first electric heating intracavitary is provided with the first heating wire, and the first electric hot plate outer surface is left
Right mutually to claim to be provided with the first of annular and connect firmly block, first matrix connects firmly the first machine on the downside of block by being arranged at described first
Frame supports on the ground.
As preferred technical solution, second reaction unit includes being arranged at the second base on the right side of first matrix
Body is provided with the second accommodating chamber in second matrix, is provided in the second accommodating chamber inner left wall and described second holds
It receives and the second of chamber unicom connects union, described second, which connects union left end, is connected to the right side inner wall of first matrix and with described
One accommodating chamber unicom, described second connects and is provided in union in the second identical pumping device of the first pumping device structure,
Second matrix outer is provided with the second electric hot plate of annular, and the second electric heating of annular is provided in second electric hot plate
Chamber, the second electric heating intracavitary are provided with the second heating wire, the second electric hot plate outer surface or so and mutually claim to be provided with annular
Second connects firmly block, and second matrix is supported on the ground by being arranged at the described second the second rack connected firmly on the downside of block.
As preferred technical solution, collection device is provided on the right side of second matrix, the collection device includes setting
The 3rd matrix being placed on the right side of second reaction unit is provided with collecting chamber, the collecting chamber and institute in the 3rd matrix
It states and collecting chamber described in unicom is provided between the second accommodating chamber and the 3rd of second accommodating chamber the connects union, the described 3rd connects connection
Threeth pumping device identical with the first pumping device structure is provided on pipe, the 3rd, which connects union right end, pierces into the collection
Intracavitary and air outlet seat is connected with, is fixedly installed and the collecting chamber unicom at end face center on the downside of the 3rd matrix
Discharging port, the discharging port are provided outside stubborn valve, priming hole, the right side of the priming hole are provided on the inner wall of the collecting chamber right side
End is provided with the 3rd cover, and the collecting chamber upper inside walls are arranged to oblique angle face, and the oblique angle face is provided with collecting pipe at center,
The collection tube outer surface is provided with gate valve, and the discharge port with the collecting chamber unicom is provided in the collecting pipe.
As preferred technical solution, first pumping device includes being fixedly connected on described first and connecing union and fix matching somebody with somebody
That closes connection connects connection ring, and described connect is provided with fixed 3rd assembling stand of fixed column in connection ring, in the 3rd assembling stand
The second electricity favourable turn is fixedly installed, the second electricity favourable turn right end is connected with fan blades by steering spindle power.
As preferred technical solution, through-hole is provided on the manganese block.
As preferred technical solution, the shock absorbing block be arranged on it is described first electricity favourable turn top and bottom and with it is described
First electricity favourable turn is fixedly connected, described to be arranged on the front-end and back-end of the first electricity favourable turn except hot fin and turn with the described first electricity
The shell of machine is fixedly connected, and the top and bottom except hot fin are fixedly connected with the shock absorbing block, the first electricity favourable turn
Front-end and back-end be respectively equipped with one group or more described except hot fin.
The beneficial effects of the invention are as follows：The configuration of the present invention is simple, easy to operate, the occupation mode of the present apparatus, user of service
It opens the second cover and passes through feeding groove toward intracavitary addition Organic Ingredients is stirred evenly, seal the second cover after addition, at this time
The oxygen for stirring evenly intracavitary is consumed by oxygen scavenger, is discharged slot at this time and is in closed state, Organic Ingredients is stirring evenly intracavitary fermentation production
Raw methane and carbon dioxide, the first electricity favourable turn start by set date, and then arm is stirred evenly by steering spindle drive and is rotated during the fermentation,
And then drive and stir evenly axis rotation, the Organic Ingredients for stirring evenly intracavitary can be stirred evenly at this time so that ferment it is more abundant, when stirring evenly
After the fermentation of intracavitary carries out a period of time, the first pumping device starts, and the second electricity favourable turn rotates at this time, and then passes through steering spindle band
Dynamic fan blades rotates, and then the methane for stirring evenly intracavitary fermentation generation and carbon dioxide are pumped into the first accommodating chamber, while passes through steaming
Steam pipe conveys vapor into the first accommodating chamber, and the first heating wire for being arranged at the first electric heating intracavitary at this time is powered and holds first
The gas of intracavitary received is heated to 960 degrees Celsius, and the vapor and methane mixed at this time is under conditions of high temperature by manganese block
Catalytic action generation carbon monoxide and hydrogen, the second pumping device starts after being reacted to greatest extent in the first accommodating chamber, into
And carbon monoxide, vapor, carbon dioxide, hydrogen and other partial gas in the first accommodating chamber are pumped into the second accommodating chamber
Interior, the second heating wire for being arranged at the second electric heating intracavitary at this time is powered and the second receiving intracavity gas is heated to 500 degrees Celsius
Temperature, carbon monoxide and vapor reacts under conditions of high temperature at this time generates hydrogen and carbon dioxide, treats the second accommodating chamber
After interior gas reacts to greatest extent the 3rd pumping device start, and then by accounted in the second accommodating chamber most of volume hydrogen, two
Carbonoxide and other a small amount of miscellaneous gas are pumped into collecting chambers, at this time by the 3rd connect union enter collecting chamber gas pass through it is advance
Limewash in injection collecting chamber carries out gas washing and washes off carbon dioxide, accounts for exhausted big portion into the gas hydrogen in collecting chamber at this time
Partial volume, and since the relative molecular mass of hydrogen is much smaller than other gases, hydrogen floats on upper strata in collecting chamber, this
When can open gate valve and pass through discharge port by hydrogen extraction can obtain more pure hydrogen, the present apparatus using a period of time
Afterwards, user of service can open the first cover and then take out the waste material for stirring evenly intracavitary, and the waste material taken out can be used as plant food
It uses, while user of service opens stubborn valve and pours out the limewash in collecting chamber and other miscellaneous gas in collecting chamber are extracted out and prepared
Next hydrogen is carried out to produce.
Description of the drawings
For ease of explanation, the present invention is described in detail by following specific embodiment and attached drawing.
Fig. 1 is a kind of internal structure schematic diagram of new volatile organic compounds control device of the present invention；
Fig. 2 is the bottom view of tank shell in Fig. 1；
Fig. 3 is the structure diagram of the first pumping device of the present invention；
Fig. 4 is the structure diagram of the manganese block of the present invention；
Fig. 5 is the external structure schematic diagram of the first electricity favourable turn in the present invention.
Specific embodiment
As Figure 1-Figure 5, a kind of new volatile organic compounds control device of the invention, including stir evenly device,
It is arranged at first reaction unit stirred evenly on the right side of device, the second reaction unit being arranged on the right side of first reaction unit
And the collection device on the right side of second reaction unit is arranged at, the device that stirs evenly includes tank shell 11, the tank shell
11 4 angles bottom is equipped with idler wheel 118 equipped with hornblock 117 and each 117 bottom of hornblock simultaneously, in the tank shell 11
It is provided with and stirs evenly chamber 45, the first assembling stand 23, first dress are fixedly installed at the center for stirring evenly 45 downside inner wall of chamber
With the first electricity favourable turn 26 is fixedly installed in seat 23,26 outside of the first electricity favourable turn is equipped with shield and carries device, and the shield carries device
Arm 24, institute are stirred evenly by steering spindle power connector with removing hot fin 262,26 upper ends of the first electricity favourable turn including shock absorbing block 261
It states and stirs evenly 24 lower face of arm or so and mutually claim and be fixedly installed to stir evenly axis 27, arm 24 is stirred evenly described in connection and is made a connection with the described first electricity
Cover net 25, the left side for stirring evenly chamber 45 and getting close to downside inner wall are provided between 26 steering spindle and first assembling stand 23
It is provided on the inner wall of side and the discharge slot 28 for stirring evenly 45 unicom of chamber, discharge 28 left end of slot is provided with the first cover 29,
It is described stir evenly chamber 45 and get close in the inner left wall of upper inside walls be fixedly installed the second assembling stand 12, on second assembling stand 12
Cavity 46 is provided with, oxygen scavenger 13 is fixedly installed between 46 upper inside walls of cavity and downside inner wall, it is described to stir evenly chamber 45
It gets close in the upper inside walls of inner left wall and is provided with feeding groove 14, be provided with the second cover 15 on the feeding groove 14, described
Mutually claim to be provided with handle 16 before and after two covers, 15 upper surface.
Valuably, first reaction unit includes being arranged at first matrix 31 stirred evenly on the right side of device, and described the
The first accommodating chamber 39 is provided in one matrix 31, is provided in 39 inner left wall of the first accommodating chamber and first accommodating chamber
The first of 39 unicom connects union 17, and described first, which connects 17 left end of union, is connected to 11 upper surface of tank shell and is stirred evenly with described
45 unicom of chamber, described first connects the first pumping device 18 is provided in union 17, and described first, which connects unicom in union 17, is provided with
Steam pipe 19, is provided with open and close valve 21 on the steam pipe 19, and described first connects the first intake valve 22, institute are provided in union 17
The manganese block 41 that annular is fixedly installed in the inner wall of the first accommodating chamber 39 is stated, the of annular is provided with outside first matrix 31
One electric hot plate 32 is provided with the first electric heating chamber 36 of annular in first electric hot plate 32, is set in the first electric heating chamber 36
There is the first heating wire 35,32 outer surface of the first electric hot plate or so mutually to claim to be provided with the first of annular and connect firmly block 34, described the
One matrix 31 is supported on the ground by being arranged at the described first the first rack 33 for connecting firmly 34 downside of block.
Valuably, second reaction unit includes the second matrix 51 for being arranged at 31 right side of the first matrix, described
The second accommodating chamber 58 is provided in second matrix 51, is provided in 58 inner left wall of the second accommodating chamber and is accommodated with described second
The second of 58 unicom of chamber connects union 37, described second connect 37 left end of union be connected to first matrix 31 right side inner wall and with
First accommodating chamber, 39 unicom, described second connect be provided in union 37 in 18 structure of the first pumping device it is identical
Two pumping devices 38 are provided with the second electric hot plate 55 of annular outside second matrix 51, are set in second electric hot plate 55
The second electric heating chamber 57 of annular is equipped with, the second heating wire 56, second electric hot plate 55 are provided in the second electric heating chamber 57
The mutual title in outer surface or so is provided with the second of annular and connects firmly block 54, and second matrix 51 connects firmly block by being arranged at described second
Second rack 53 of 54 downsides supports on the ground.
Valuably, second matrix, 51 right side is provided with collection device, and the collection device includes being arranged at described the
The 3rd matrix 77 on the right side of two reaction units, is provided with collecting chamber 78 in the 3rd matrix 77, the collecting chamber 78 with it is described
The 3rd of collecting chamber 78 described in unicom and second accommodating chamber 58 is provided between second accommodating chamber 58 and connects union 62, described
Three connect threeth pumping device 61 identical with 18 structure of the first pumping device are provided in union 62, and the 3rd to connect union 62 right
End is pierced into the collecting chamber 78 and is connected with air outlet seat 63, is fixedly installed at the 77 downside end face center of the 3rd matrix
There is a discharging port 66 with 78 unicom of collecting chamber, the discharging port 66 is provided outside stubborn valve 67, in 78 right side of collecting chamber
Priming hole 68 is provided on wall, the right end of the priming hole 68 is provided with the 3rd cover 69, and 78 upper inside walls of collecting chamber are set
Oblique angle face 73 is set to, collecting pipe 74 is provided at 73 center of oblique angle face, 74 outer surface of collecting pipe is provided with gate valve 76,
The discharge port 75 with 78 unicom of collecting chamber is provided in the collecting pipe 74.
Valuably, first pumping device 18 connects the connection of 17 secure fit of union including being fixedly connected on described first
Connection ring 91 is connect, described connect in connection ring 91 is provided with 92 fixed 3rd assembling stand 93 of fixed column, the 3rd assembling stand 93
The second electricity favourable turn 94 is inside fixedly installed, the second electricity 94 right ends of favourable turn are connected with fan blades 95 by steering spindle power.
Valuably, it is provided with through-hole 43 on the manganese block 41.
Valuably, the shock absorbing block 261 be arranged on it is described first electricity favourable turn 26 top and bottom and with described first electricity
Favourable turn 26 is fixedly connected, it is described except hot fin 262 be arranged on the front-end and back-end of the first electricity favourable turn 26 and with the described first electricity
The shell of favourable turn 26 is fixedly connected, and the top and bottom except hot fin 262 are fixedly connected with the shock absorbing block 261, described
The front-end and back-end of first electricity favourable turn 26 are respectively equipped with one group or more described except hot fin 262, it is described except hot fin 262 absorbing
And the heat that generates when distributing the first electricity 26 operation of favourable turn, the shock absorbing block 261 is reducing the first electricity favourable turn 26
The shaking force operationally generated prevents that shaking force is excessive and influences the normal operation of the present apparatus.
The occupation mode of the present apparatus, user of service open the second cover 15 and pass through feeding groove 14 and add toward stirring evenly in chamber 45
Organic Ingredients seals the second cover 15 after addition, and the oxygen stirred evenly at this time in chamber 45 is consumed by oxygen scavenger 13, at this time
Discharge slot 28 is in closed state, and Organic Ingredients is stirring evenly fermentation generation methane and carbon dioxide in chamber 45, during the fermentation
First electricity 26 start by set date of favourable turn, and then arm 24 is stirred evenly by steering spindle drive and is rotated, and then drive stirs evenly axis 27 and rotates, at this time
The Organic Ingredients stirred evenly in chamber 45 can be stirred evenly so that ferment it is more abundant, when stir evenly the fermentation in chamber 45 carry out one section when
Between after, the first pumping device 18 starts, at this time second electricity favourable turn 94 rotate, and then by steering spindle drive fan blades 95 rotate, into
And fermentation generates in chamber 45 methane will be stirred evenly and carbon dioxide is pumped into the first accommodating chamber 39, while by steam pipe 19 to the
Conveying vapor in one accommodating chamber 39, the first heating wire 35 being arranged at this time in the first electric heating chamber 36 are powered and are accommodated first
Gas in chamber 39 is heated to 960 degrees Celsius, and the vapor and methane mixed at this time is under conditions of high temperature by manganese block
41 catalytic action generation carbon monoxide and hydrogen, second pumping device 38 opens after being reacted to greatest extent in the first accommodating chamber 39
It is dynamic, and then carbon monoxide, vapor, carbon dioxide, hydrogen and other partial gas in the first accommodating chamber 39 are pumped into the
In two accommodating chambers 58, the second heating wire 56 being arranged at this time in the second electric heating chamber 57 is powered and by gas in the second accommodating chamber 58
500 degrees Celsius of temperature is heated to, carbon monoxide reacts generation hydrogen and titanium dioxide with vapor under conditions of high temperature at this time
Carbon, the 3rd pumping device 61 starts after gas reacts to greatest extent in the second accommodating chamber 58, and then will be in the second accommodating chamber 58
The hydrogen, carbon dioxide and other a small amount of miscellaneous gas for accounting for most of volume are pumped into collecting chamber 78, connect union by the 3rd at this time
62 gases for entering collecting chamber 78 carry out gas washing by the limewash being previously implanted in collecting chamber 78 and wash off carbon dioxide, at this time
Most volumes are accounted for into the gas hydrogen in collecting chamber 78, and since the relative molecular mass of hydrogen is much smaller than other gas
Body, therefore hydrogen floats on upper strata in collecting chamber 78, can open gate valve 76 at this time and pass through discharge port 75 and extract hydrogen out
More pure hydrogen is obtained, after the present apparatus is using a period of time, user of service can open the first cover 29 and then will stir evenly
Waste material in chamber 45 takes out, and the waste material taken out can be used as plant food, while user of service opens and twists valve 67 by collection
Limewash in chamber 78 is poured out and extracts and be ready for next hydrogen other miscellaneous gas in collecting chamber 78 out and produces.
The beneficial effects of the invention are as follows：The configuration of the present invention is simple, easy to operate, the occupation mode of the present apparatus, user of service
It opens the second cover and passes through feeding groove toward intracavitary addition Organic Ingredients is stirred evenly, seal the second cover after addition, at this time
The oxygen for stirring evenly intracavitary is consumed by oxygen scavenger, is discharged slot at this time and is in closed state, Organic Ingredients is stirring evenly intracavitary fermentation production
Raw methane and carbon dioxide, the first electricity favourable turn start by set date, and then arm is stirred evenly by steering spindle drive and is rotated during the fermentation,
And then drive and stir evenly axis rotation, the Organic Ingredients for stirring evenly intracavitary can be stirred evenly at this time so that ferment it is more abundant, when stirring evenly
After the fermentation of intracavitary carries out a period of time, the first pumping device starts, and the second electricity favourable turn rotates at this time, and then passes through steering spindle band
Dynamic fan blades rotates, and then the methane for stirring evenly intracavitary fermentation generation and carbon dioxide are pumped into the first accommodating chamber, while passes through steaming
Steam pipe conveys vapor into the first accommodating chamber, and the first heating wire for being arranged at the first electric heating intracavitary at this time is powered and holds first
The gas of intracavitary received is heated to 960 degrees Celsius, and the vapor and methane mixed at this time is under conditions of high temperature by manganese block
Catalytic action generation carbon monoxide and hydrogen, the second pumping device starts after being reacted to greatest extent in the first accommodating chamber, into
And carbon monoxide, vapor, carbon dioxide, hydrogen and other partial gas in the first accommodating chamber are pumped into the second accommodating chamber
Interior, the second heating wire for being arranged at the second electric heating intracavitary at this time is powered and the second receiving intracavity gas is heated to 500 degrees Celsius
Temperature, carbon monoxide and vapor reacts under conditions of high temperature at this time generates hydrogen and carbon dioxide, treats the second accommodating chamber
After interior gas reacts to greatest extent the 3rd pumping device start, and then by accounted in the second accommodating chamber most of volume hydrogen, two
Carbonoxide and other a small amount of miscellaneous gas are pumped into collecting chambers, at this time by the 3rd connect union enter collecting chamber gas pass through it is advance
Limewash in injection collecting chamber carries out gas washing and washes off carbon dioxide, accounts for exhausted big portion into the gas hydrogen in collecting chamber at this time
Partial volume, and since the relative molecular mass of hydrogen is much smaller than other gases, hydrogen floats on upper strata in collecting chamber, this
When can open gate valve and pass through discharge port by hydrogen extraction can obtain more pure hydrogen, the present apparatus using a period of time
Afterwards, user of service can open the first cover and then take out the waste material for stirring evenly intracavitary, and the waste material taken out can be used as plant food
It uses, while user of service opens stubborn valve and pours out the limewash in collecting chamber and other miscellaneous gas in collecting chamber are extracted out and prepared
Next hydrogen is carried out to produce.
The above description is merely a specific embodiment, but protection scope of the present invention is not limited thereto, any
The change or replacement expected without creative work, should be covered by the protection scope of the present invention.Therefore, it is of the invention
Protection domain should be determined by the scope of protection defined in the claims.
Claims (7)
1. a kind of new volatile organic compounds control device, including stirring evenly device, being arranged at described stir evenly on the right side of device
First reaction unit, the second reaction unit being arranged on the right side of first reaction unit and be arranged at it is described second reaction dress
Put the collection device on right side, the device that stirs evenly includes tank shell, and tank shell four angles bottom is simultaneously equipped with hornblock and every
A hornblock bottom is equipped with idler wheel, is provided in the tank shell and stirs evenly chamber, described to stir evenly on the downside of chamber at the center of inner wall
The first assembling stand is fixedly installed, the first electricity favourable turn, the first electricity favourable turn outside are fixedly installed in first assembling stand
Equipped with shield load device, the shield carries device and passes through steering spindle power with removing hot fin, the first electricity favourable turn upper end including shock absorbing block
Be connected with and stir evenly arm, the described arm lower face or so that stirs evenly mutually claims and is fixedly installed to stir evenly axis, stirred evenly described in connection arm with it is described
Cover net is provided between the steering spindle of first electricity favourable turn and first assembling stand, the chamber that stirs evenly gets close to downside inner wall
Be provided in inner left wall with the discharge slot for stirring evenly chamber unicom, it is described discharge slot left end be provided with the first cover, it is described to stir
Even chamber, which is got close in the inner left wall of upper inside walls, is fixedly installed the second assembling stand, and cavity is provided on second assembling stand,
Oxygen scavenger is fixedly installed between the cavity upper inside walls and downside inner wall, the chamber that stirs evenly is got close in the upside of inner left wall
Feeding groove is provided on wall, the second cover is provided on the feeding groove, mutually claims to be provided with before and after the second cover upper surface
Handle.
2. a kind of new volatile organic compounds control device according to claim 1, it is characterised in that：Described first
Reaction unit includes being arranged at first matrix stirred evenly on the right side of device, and the first accommodating chamber is provided in first matrix,
It is provided in the first accommodating chamber inner left wall and connects union with the first of the first accommodating chamber unicom, described first connects union
Left end is connected to the tank shell upper surface and stirs evenly chamber unicom with described, and described first connects and first is provided in union pumps dress
It puts, described first, which connects unicom in union, is provided with steam pipe, open and close valve is provided on the steam pipe, described first connects in union
The first intake valve is provided with, the manganese block of annular, first matrix outer are fixedly installed in the inner wall of first accommodating chamber
The first electric hot plate of annular is provided with, the first electric heating chamber of annular, the first electric heating chamber are provided in first electric hot plate
It is inside provided with the first heating wire, the first electric hot plate outer surface or so and mutually claims to be provided with the first of annular and connect firmly block, described the
One matrix is supported on the ground by being arranged at the described first the first rack connected firmly on the downside of block.
3. a kind of new volatile organic compounds control device according to claim 1, it is characterised in that：Described second
Reaction unit includes being arranged at the second matrix on the right side of first matrix, and the second accommodating chamber is provided in second matrix,
It is provided in the second accommodating chamber inner left wall and connects union with the second of the second accommodating chamber unicom, described second connects union
Left end is connected to the right side inner wall of first matrix and connects and be provided in union with the first accommodating chamber unicom, described second
In the second identical pumping device of the first pumping device structure, second matrix outer is provided with the second electric heating of annular
Plate, the second electric heating chamber of annular is provided in second electric hot plate, and the second electric heating intracavitary is provided with the second heating wire, institute
It states second electric hot plate outer surface or so and mutually claims to be provided with the second of annular and connect firmly block, second matrix is by being arranged at described the
Two the second racks for connecting firmly on the downside of block support on the ground.
4. a kind of new volatile organic compounds control device according to claim 1, it is characterised in that：Described second
Collection device is provided on the right side of matrix, the collection device includes being arranged at the 3rd matrix on the right side of second reaction unit,
Collecting chamber is provided in 3rd matrix, collecting chamber described in unicom is provided between the collecting chamber and second accommodating chamber
And the 3rd of second accommodating chamber connects union, the described 3rd connect be provided in union it is identical with the first pumping device structure
The 3rd pumping device, the 3rd, which connects union right end, pierces into the collecting chamber and is connected with air outlet seat, the 3rd matrix
The discharging port with the collecting chamber unicom is fixedly installed at the end face center of downside, the discharging port is provided outside stubborn valve, described
Be provided with priming hole on the right side of collecting chamber on inner wall, the right end of the priming hole is provided with the 3rd cover, on the upside of the collecting chamber in
Wall is arranged to oblique angle face, and collecting pipe is provided at the center of the oblique angle face, and the collection tube outer surface is provided with gate valve, the receipts
The discharge port with the collecting chamber unicom is provided in collector.
5. a kind of new volatile organic compounds control device according to claim 1, it is characterised in that：Described first
Pumping device include being fixedly connected on described first connect the connection of union secure fit connect connection ring, it is described connect be provided in connection ring it is logical
Fixed 3rd assembling stand of fixed column is crossed, the second electricity favourable turn, the second electricity favourable turn are fixedly installed in the 3rd assembling stand
Right end is connected with fan blades by steering spindle power.
6. a kind of new volatile organic compounds control device according to claim 1, it is characterised in that：The manganese block
On be provided with through-hole.
7. a kind of new volatile organic compounds control device according to claim 1, it is characterised in that：The shock absorbing
Block is arranged on the top and bottom of the first electricity favourable turn and is fixedly connected with the described first electricity favourable turn, described except hot fin is arranged on
The front-end and back-end of the first electricity favourable turn and be fixedly connected with the shell of the described first electricity favourable turn, the upper end except hot fin with
Lower end is fixedly connected with the shock absorbing block, and the front-end and back-end of the first electricity favourable turn are respectively equipped with one group or more described and remove
Hot fin.
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| CN201810130825.3A CN108083227B (en) | 2018-02-08 | 2018-02-08 | A kind of novel volatile organic compounds control device |
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| CN108083227B CN108083227B (en) | 2019-01-25 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108328575A (en) * | 2018-02-08 | 2018-07-27 | 宁德市安升环保科技有限公司 | A kind of volatile organic compounds control device |
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|---|---|---|---|---|
| US20140157991A1 (en) * | 2012-12-09 | 2014-06-12 | Chun-Rei Yang | Environmentally-friendly Exhaust Device |
| CN205933583U (en) * | 2016-07-28 | 2017-02-08 | 河南越宝生物科技有限公司 | Mud waste gas recovery mummification machine |
| CN107166578A (en) * | 2017-07-07 | 2017-09-15 | 黄山市雅龙智能科技有限公司 | A kind of air cleaning unit |
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| CN108083227B (en) | 2019-01-25 |
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Address after: 325600 No. 298, wei16 Road, Yueqing Economic Development Zone, Yueqing City, Zhejiang Province Patentee after: JIANGSHAN HUALUNG ENERGY DEVELOPMENT LTD. Address before: 324112, No. 5, No. 1, fire protection base, Xintang Town, Jiangshan, Zhejiang, Quzhou Patentee before: JIANGSHAN HUALUNG ENERGY DEVELOPMENT LTD. |
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Effective date of registration: 20200528 Address after: No. 516, South Road, Haian Town, Haian City, Nantong City, Jiangsu Province Patentee after: JIANGSU JIAYU SPECIAL EQUIPMENT Co.,Ltd. Address before: No.428, South Road, Haian high tech Zone (former Haian town), Haian City, Nantong City, Jiangsu Province Patentee before: Nantong doctoral innovation technology transfer Co.,Ltd. Effective date of registration: 20200528 Address after: No.428, South Road, Haian high tech Zone (former Haian town), Haian City, Nantong City, Jiangsu Province Patentee after: Nantong doctoral innovation technology transfer Co.,Ltd. Address before: 325600 No. 298, wei16 Road, Yueqing Economic Development Zone, Yueqing City, Zhejiang Province Patentee before: JIANGSHAN HUALUNG ENERGY DEVELOPMENT Ltd. |
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Denomination of invention: A new control device for volatile organic compounds Effective date of registration: 20210528 Granted publication date: 20190125 Pledgee: Bank of China Limited by Share Ltd. Haian branch Pledgor: JIANGSU JIAYU SPECIAL EQUIPMENT Co.,Ltd. Registration number: Y2021980004154 |