CN204848883U - Jar of oil ferment fermentation organic medium release internal energy - Google Patents
Jar of oil ferment fermentation organic medium release internal energy Download PDFInfo
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- CN204848883U CN204848883U CN201520466838.XU CN201520466838U CN204848883U CN 204848883 U CN204848883 U CN 204848883U CN 201520466838 U CN201520466838 U CN 201520466838U CN 204848883 U CN204848883 U CN 204848883U
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Abstract
The utility model belongs to an alkane brewing equipment field especially relates to a jar of oil ferment fermentation organic medium release internal energy, change the factor backward flow condiment post (5), gaseous phase chamber (6), liquid phase chamber (7), be full of thermal stress annular space pipe (9), difference frequency local oscillator post (11), demister (12), casing (13) and difference frequency reflux unit (14) including alternately flow state reaction tube (1), catalytic reaction pipe (2), distil off tub (3), the gaseous flow state reformation generation unit (4) of hydro carbons, two hydrogen, hydro carbons gaseous flow state reformation generation unit (4) upper end with intersect flow state reaction tube (1) fix and communicate with each other, lower extreme and casing (13) communicate with each other, two hydrogen commentaries on classics factor backward flow condiment posts (5) just communicate with each other with casing (13) inner chamber on being located casing (13), the both ends of catalytic reaction pipe (2) with intersect flow state reaction tube (1) communicate with each other. The utility model discloses the low energy consumption, the low cost, low dangerous, environmental protection efficiency is showing.
Description
Technical field
The utility model belongs to alkane brewing equipment field, particularly relates to the tank of energy in the release of a kind of oil ferment fermentation organic medium.
Background technology
China's energy development is faced with multiple predicament.First, energy expenditure increases fast, and power supply also wants corresponding growth, but power supply increment continues main dependence coal and Imported oil.Secondly, although China has formulated energy-saving and emission-reduction policy and target, effects of energy saving and emission reduction has been subject to the challenge of GDP speedup.Again, Energy restructuring is made slow progress, and coal accounting is high remains realistic problem.These factors result in China's energy prices continue soaring, energy environment pressure constantly increases, energy security faces multiple challenges.
China's energy structure " congenital defect ", this natural endowment being also we often say is tired.Since this century, China's total energy consumption rises rapidly, main dependence coal and oil, Sweet natural gas.Present China has become one of maximum in the world energy expenditure state, but the speed that rises of China's Energy production amount rises soon not as consumption simultaneously, and wherein, oil consumption rate of growth increases apparently higher than output in domestic.China is only second to the U.S., is the second-biggest-in-the-world oil consuming countries.Sweet natural gas and non-fossil energy (water power, nuclear power and wind-powered electricity generation) turnout rapid development in recent years, but total amount is still limited.The energy and related infrastructure are invested huge, and within 2010, investment is more than 2 trillion yuan Renminbi, and it is over half that power construction account for all energy investments, is secondly oil and gas exploitation, are petrochemical industry investment again.
Under China's energy expenditure increases too fast prerequisite, china natural resources environmental stress is huge, be difficult to continue.Continue the prerequisite risen in demand under, the price of international energy will continue to rise, and energy security problem will constantly show especially, and home and abroad environment constraint will constantly be strengthened.
World's oil resources concentrates on a few countries, and exploitation difficulty is also increasing.World's oil resources and geopolitical condition make the increase of world oil output be subject to obvious restriction, can only maintain average year and increase about 1%.
At present, our oil refining process or a high energy consumption, high cost, the production technique of high-risk.Part oil field, industrial waste remain quite a few deposition heavy hydrocarbon resources.How to utilize above-mentioned recyclable materials, to solution energy shortage and problem of environmental pollution significant.
Utility model content
The utility model is intended to overcome the deficiencies in the prior art part and provides a kind of structure simple, less energy-consumption, low cost, low danger, the tank of energy in the release of environmental protection efficacy significant oil ferment fermentation organic medium.
For solving the problems of the technologies described above, the utility model realizes like this.
In the release of oil ferment fermentation organic medium can a tank, it comprise intersect fluidised form reaction tubes, catalytic reaction tube, distillate pipe, hydrocarbon gas fluidised form reformation generating unit, two hydrogen transfer factor reflux condiment post, gas phase chamber, liquid phase cavity, be full of thermal stresses annular space pipe, difference frequency local oscillator post, foam breaking mesh, housing and difference frequency reflux unit; Described hydrocarbon gas fluidised form reformation generating unit divides two groups; Often group comprises 4 cylinders, its upper end respectively with intersect fluidised form reaction tubes and fixedly communicate, its lower end fixedly communicates with housing respectively; Described foam breaking mesh is laterally fixedly placed in housing, makes housing cavity be divided into gas phase chamber and liquid phase cavity up and down; Described difference frequency local oscillator post connects with the lower vertical of foam breaking mesh; Described pair of hydrogen transfer factor backflow condiment post is fixed on housing, and communicates with housing cavity; Reflux with the two hydrogen transfer factor respectively top of condiment post and housing cavity of the two ends of described difference frequency reflux unit communicates; The two ends of described catalytic reaction tube with intersect fluidised form reaction tubes and communicate; Describedly distillate pipe and intersect fluidised form reaction tubes and communicate; The described thermal stresses annular space pipe that is full of is fixed at the bottom of housing.
As a kind of preferred version, the utility model on the housing portion is provided with temperature control induction installation.
Further, the utility model can be provided with tank internal pressure setter in portion on the housing.
The utility model structure is simple, and less energy-consumption, low cost, low danger, environmental protection efficacy is remarkable.Only can complete traditional oil refining process with one or several equipment needs several tall and big distillation towers, the production process that process furnace just can complete.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.Protection domain of the present utility model is not only confined to the statement of following content.
Fig. 1 is internal structure schematic diagram of the present utility model.
Fig. 2 is side-view of the present utility model.
In figure: 1, intersection fluidised form reaction tubes; 2, catalytic reaction tube; 3, pipe is distillated; 4, hydrocarbon gas fluidised form reformation generating unit; 5, two hydrogen transfer factor backflow condiment post; 6, gas phase chamber; 7, liquid phase cavity; 8, slag-drip opening; 9, thermal stresses annular space pipe is full of; 10, heat absorbing units; 11, difference frequency local oscillator post; 12, foam breaking mesh; 13, housing; 14, difference frequency reflux unit; 15, temperature control induction installation; 16, tank internal pressure setter.
Embodiment
As shown in the figure, in the release of oil ferment fermentation organic medium can a tank, comprise intersect fluidised form reaction tubes 1, catalytic reaction tube 2, distillate pipe 3, hydrocarbon gas fluidised form reformation generating unit 4, two hydrogen transfer factor backflow condiment post 5, gas phase chamber 6, liquid phase cavity 7, be full of thermal stresses annular space pipe 9, difference frequency local oscillator post 11, foam breaking mesh 12, housing 13 and difference frequency reflux unit 14; Described hydrocarbon gas fluidised form reformation generating unit 4 points two groups; Often group comprises 4 cylinders, its upper end respectively with intersect fluidised form reaction tubes 1 and fixedly communicate, its lower end fixedly communicates with housing 13 respectively; Described foam breaking mesh 12 is laterally fixedly placed in housing 13, makes housing 13 inner chamber be divided into gas phase chamber 6 and liquid phase cavity 7 up and down; Described difference frequency local oscillator post 11 connects with the lower vertical of foam breaking mesh 12; Described pair of hydrogen transfer factor backflow condiment post 5 is fixed on housing 13, and communicates with housing 13 inner chamber; Reflux with the two hydrogen transfer factor respectively top of condiment post 5 and housing 13 inner chamber of the two ends of described difference frequency reflux unit 14 communicates; The two ends of described catalytic reaction tube 2 with intersect fluidised form reaction tubes 1 and communicate; Describedly distillate pipe 3 and intersect fluidised form reaction tubes 1 and communicate; The described thermal stresses annular space pipe 9 that is full of is fixed at the bottom of housing 13.
The utility model is provided with temperature control induction installation 15 on described housing 13 top.The utility model is provided with tank internal pressure setter 16 on described housing 13 top.
When concrete operations, filling zirconium white in hydrocarbon gas fluidised form reformation generating unit 4; Aluminum oxide is loaded in catalytic reaction tube 2; Niobium molybdenum alloy is loaded in two hydrogen transfer factor backflow condiment post 5.The straw hydrocarbon of 30% is mixed with 70% heavy oil, puts into aforesaid device.Brewage C
8-C
24, vaporize when temperature reaches when 84-284 spends, fail by lifting force recombinant C at heat space
8-C
24, or be greater than C
8-C
24hydrocarbon molecules group, a part is kept off back by gas flow pattern reformation generating unit 4, feeds back backflow through foam breaking mesh 12, and another part, by two hydrogen transfer factor backflow condiment post 5, feeds back through foam breaking mesh 12 and refluxes.Major part returns liquid phase along difference frequency local oscillator post 11, because the temperature and the liquid phase temperature difference feeding back the hydrocarbons of backflow is comparatively large, therefore causes liquid phase fluid material generation local oscillator in tank, accelerates enzymatic reaction, press the C of lifting force restructuring at heat space
8-C
24hydrocarbon molecules group, through being equipped with zirconic hydrocarbon gas fluidised form reformation generating unit 4, intersecting fluidised form reaction tubes 1, catalytic reaction tube 2 and produces refining C
8-C
24.The utility model temperature control induction installation 16 can control the envrionment temperature of tank body; Tank internal pressure setter can control the pressure parameter of tank body.
The foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, for a person skilled in the art, the utility model can have various modifications and variations.All within spirit of the present utility model and principle, any amendment done, equivalent replacement, improvement etc., all should be included within protection domain of the present utility model.
Claims (3)
1. the tank of the interior energy of oil ferment fermentation organic medium release, it is characterized in that, comprise intersect fluidised form reaction tubes (1), catalytic reaction tube (2), distillate pipe (3), hydrocarbon gas fluidised form reformation generating unit (4), two hydrogen transfer factor reflux condiment post (5), gas phase chamber (6), liquid phase cavity (7), be full of thermal stresses annular space pipe (9), difference frequency local oscillator post (11), foam breaking mesh (12), housing (13) and difference frequency reflux unit (14); Described hydrocarbon gas fluidised form reformation generating unit (4) divides two groups; Often group comprises 4 cylinders, its upper end respectively with intersect fluidised form reaction tubes (1) and fixedly communicate, its lower end fixedly communicates with housing (13) respectively; Described foam breaking mesh (12) is laterally fixedly placed in housing (13), makes housing (13) inner chamber be divided into gas phase chamber (6) and liquid phase cavity (7) up and down; Described difference frequency local oscillator post (11) connects with the lower vertical of foam breaking mesh (12); Described pair of hydrogen transfer factor backflow condiment post (5) is fixed on housing (13), and communicates with housing (13) inner chamber; Reflux with the two hydrogen transfer factor respectively top of condiment post (5) and housing (13) inner chamber of the two ends of described difference frequency reflux unit (14) communicates; The two ends of described catalytic reaction tube (2) with intersect fluidised form reaction tubes (1) and communicate; Describedly distillate pipe (3) and intersect fluidised form reaction tubes (1) and communicate; The described thermal stresses annular space pipe (9) that is full of is fixed at the bottom of housing (13).
2. the tank of the interior energy of oil ferment fermentation organic medium release according to claim 1, is characterized in that: be provided with temperature control induction installation (15) on described housing (13) top.
3. the tank of the interior energy of oil ferment fermentation organic medium release according to claim 2, is characterized in that: be provided with tank internal pressure setter (16) on described housing (13) top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520466838.XU CN204848883U (en) | 2015-07-02 | 2015-07-02 | Jar of oil ferment fermentation organic medium release internal energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520466838.XU CN204848883U (en) | 2015-07-02 | 2015-07-02 | Jar of oil ferment fermentation organic medium release internal energy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204848883U true CN204848883U (en) | 2015-12-09 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520466838.XU Expired - Fee Related CN204848883U (en) | 2015-07-02 | 2015-07-02 | Jar of oil ferment fermentation organic medium release internal energy |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204848883U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106929413A (en) * | 2017-03-01 | 2017-07-07 | 姜国文 | Chicken manure terpene straw hydrocarbon prepares alkane brewing equipment and its technique |
-
2015
- 2015-07-02 CN CN201520466838.XU patent/CN204848883U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106929413A (en) * | 2017-03-01 | 2017-07-07 | 姜国文 | Chicken manure terpene straw hydrocarbon prepares alkane brewing equipment and its technique |
| CN106929413B (en) * | 2017-03-01 | 2023-03-17 | 姜国文 | Brewing equipment and process for preparing alkane from chicken manure terpenized grass hydrocarbon |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20151209 Termination date: 20180702 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |