CN107008212A - Light hydrocarbon reactor - Google Patents
Light hydrocarbon reactor Download PDFInfo
- Publication number
- CN107008212A CN107008212A CN201510911961.2A CN201510911961A CN107008212A CN 107008212 A CN107008212 A CN 107008212A CN 201510911961 A CN201510911961 A CN 201510911961A CN 107008212 A CN107008212 A CN 107008212A
- Authority
- CN
- China
- Prior art keywords
- light hydrocarbon
- heating
- heating plate
- inlet pipe
- heating surface
- 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
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/0006—Controlling or regulating processes
- B01J19/0013—Controlling the temperature of the process
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00076—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements inside the reactor
- B01J2219/00085—Plates; Jackets; Cylinders
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention discloses a kind of light hydrocarbon reactor, including：Tank body, the heating plate in tank body and the oil inlet pipe installed in heating plate one end, the heating plate includes a heating surface, the heating surface with respect to the horizontal plane has certain gradient, the oil inlet pipe is arranged on the slightly higher one end of the heating surface, and above the heating surface, some oil outlets are provided with the section that the oil inlet pipe is located on heating surface.Light hydrocarbon reactor of the present invention, the heating plate of certain gradient and certain heating surface (area) (HS is installed in tank interior, make liquid light hydrocarbon flow through heater plate surface just in time to be gasified, and by controlling the flow of liquid light hydrocarbon to can control the amount of vaporization of whole reactor, so as to ensure the stable supplying of different usage amount situations.
Description
Technical field
The present invention relates to gas burning field, more particularly to a kind of light hydrocarbon reactor.
Background technology
Usually said lighter hydrocarbons are light dydrocarbon, also known as pentane, there is pentane, three kinds of isomers of isopentane and neopentane.Lighter hydrocarbons are the products of oil refining, are liquid at normal temperatures and pressures.Liquid light hydrocarbon can meet the occasion that atm number uses combustion gas after gasification, such as：Gas oven, blast furnace, gas fired-boiler, bulb manufacturing, glass container production industry and various electronic kilns, etc.；Small tolerance occasion is can also be used for, such as：Hotel, wineshop, school, office, army and civil kitchen range, etc..
Light hydrocarbon air mixture generation system is no lack of in published patent document to be seen in, and is the core apparatus of whole system by the reactor that liquid light hydrocarbon gasifies in whole fuel gas generating system.Existing gasification mode mainly has：A kind of is that the liquid light hydrocarbon for being stored in reactor is heated using heating medium such as water, i.e., by the way of " water proof boiling " gasification, this mode is safer, but is detrimental to save the energy；It is thus existing that direct-fired mode is carried out to the liquid light hydrocarbon of storage in a kettle. using the heating element heater being located in reactor, it is all that the liquid light hydrocarbon of certain storage is heated that this direct-fired mode and the before mode of " water proof boiling ", which are heated, this mode of heating needs to heat the liquid light hydrocarbon of whole storage, thus heat slow, and the bad control of heating and gasifying amount, the generator yield that thus system occurs for whole light hydrocarbon air mixture is certain, need to store unnecessary combustion gas during for demand tolerance less, for demand it is large-minded when, need to increase the volume of reactor, to store more liquid light hydrocarbons.Whole system huge structure can thus be made, cost becomes big.
The content of the invention
The present invention solves the technical problem of a kind of light hydrocarbon reactor is provided, the stable supplying of different usage amount situations ensure that.
In order to solve the above technical problems, one aspect of the present invention is：A kind of tank body, the heating plate in tank body and the oil inlet pipe installed in heating plate one end are provided, the heating plate includes a heating surface, the heating surface with respect to the horizontal plane has certain gradient, the oil inlet pipe is arranged on the slightly higher one end of the heating surface, and above the heating surface, some oil outlets are provided with the section that the oil inlet pipe is located on heating surface.
In a preferred embodiment of the present invention, the reactor includes polylith heating plate, and the heating plate is placed in stacking.
In a preferred embodiment of the present invention, every piece of heating plate correspondence installs an oil inlet pipe.
In a preferred embodiment of the present invention, the inclination range of the heating surface is to be less than or equal to 45 ° more than 0 °.
In a preferred embodiment of the present invention, the tank body is cuboid or cylinder or other shapes for having an inner chamber.
In a preferred embodiment of the present invention, the tank body is the tank body of the hemispherical inner chamber in left and right ends.
In a preferred embodiment of the present invention, the reactor also includes air inlet pipe, and the air inlet pipe is located at the heating plate top or bottom.
In a preferred embodiment of the present invention, the heating plate includes having heating medium in internal cavities, the internal cavities.
In a preferred embodiment of the present invention, heating plate upper surface temperature is more than 36 DEG C.
The beneficial effects of the invention are as follows：Light hydrocarbon reactor of the present invention, the heating plate of certain gradient and certain heating surface (area) (HS is installed in tank interior, make liquid light hydrocarbon flow through heater plate surface just in time to be gasified, and by controlling the flow of liquid light hydrocarbon to can control the amount of vaporization of whole reactor, so as to ensure the stable supplying of different usage amount situations.
Brief description of the drawings
Fig. 1 is the structural representation of the preferred embodiment of light hydrocarbon reactor one of the present invention；
Fig. 2 is the structural representation of another preferred embodiment of light hydrocarbon reactor of the present invention；
Fig. 3 is the structural representation of the another preferred embodiment of light hydrocarbon reactor of the present invention；
Fig. 4 is the structural representation of light hydrocarbon reactor another embodiment of the present invention.
Embodiment
Presently preferred embodiments of the present invention is described in detail below in conjunction with the accompanying drawings, so that advantages and features of the invention can be easier to be readily appreciated by one skilled in the art, apparent clearly defined so as to be made to protection scope of the present invention.
Referring to Fig. 1, the embodiment of the present invention includes：
A kind of light hydrocarbon reactor, including：Tank body 1, heating plate 2 and oil inlet pipe 3.
The tank body 1 includes oil inlet and gas outlet 11.
Heating plate 2 described in the heating plate 2 is arranged in the tank body 1, and the heating plate 2 includes a heating surface 21 for having certain surface to accumulate, and the heating surface 21 has certain gradient, and the heating surface can be plane or cambered surface.The inclination range of the heating surface 21 is most preferably more than 0 ° and is less than or equal to 45 °.The section of heating plate 2 is except the rectangle shown in embodiment and taper, or cone, or triangle, or polygon.The heating plate 2 can also include having heating medium in internal cavities 22, the internal cavities 22, and the heating medium can be water or other heating media.This mode using heating medium indirectly heat is safer, naturally it is also possible to use other mode of heatings.
The oil inlet pipe 3 is extended in the tank body 1 from oil inlet 11, and the oil inlet pipe 3 is arranged on the slightly higher one end of the heating surface 21, and above the heating surface 21, some oil outlets 31 are provided with the section that the oil inlet pipe 3 is located on heating surface 21.
The course of work of this implementation light hydrocarbon reactor is as follows：The heating plate 2 is heated to required temperature, and the oil inlet pipe 3 starts into liquid light hydrocarbon, and the liquid light hydrocarbon flows through the heating surface 21 of the heating plate 2 by oil outlet 31, the liquid light hydrocarbon heating and gasifying, and lighter hydrocarbons flow out tank body through gas outlet after gasification.By the gas output for controlling the oil inlet quantity of oil inlet pipe 3 and the temperature of heating plate 2 and then control gaseous state lighter hydrocarbons.
The light hydrocarbon reactor of another preferred embodiment shown in Fig. 2, the present embodiment light hydrocarbon reactor includes polylith heating plate, and the heating plate is placed in stacking；Every piece of heating plate correspondence installs an oil inlet pipe.The form that this stacking is placed, can more save space, increase efficiency, and oil-control valve can be respectively mounted at oil inlet pipe, by controlling the flow of each oil inlet pipe to control the gas output scope of the reactor respectively.
The light hydrocarbon reactor of further embodiment shown in Fig. 3, the present embodiment light hydrocarbon reactor also includes an air inlet pipe 4, and the air inlet pipe 4 is located at the top of heating plate 2 or bottom, and the air inlet pipe 4 shown in the present embodiment is located at the bottom of heating plate 2.The inwall of the heating plate 2 and the tank body 1 has space, and air can be passed through in tank body 1 by the air inlet pipe 4, is blended directly in through the space and gaseous state lighter hydrocarbons in reactor and directly forms lighter hydrocarbons air mixture.
Fig. 4 show example IV, the hemispherical inner chamber in left and right ends of the tank body 1, and such air, which enters tank body, to be reflected in through inner tank wall on heating surface 21, so as to gaseous state lighter hydrocarbons mix it is more uniform.
Light hydrocarbon reactor of the present invention, the heating plate of certain gradient and certain heating surface (area) (HS is installed in tank interior, make liquid light hydrocarbon flow through heater plate surface just in time to be gasified, and by controlling the flow of liquid light hydrocarbon to can control the amount of vaporization of whole reactor, so as to ensure the stable supplying of different usage amount situations.
It the foregoing is only embodiments of the invention; it is not intended to limit the scope of the invention; equivalent structure or equivalent flow conversion that every utilization description of the invention and accompanying drawing content are made; or other related technical fields are directly or indirectly used in, it is included within the scope of the present invention.
Claims (9)
1. a kind of light hydrocarbon reactor, it is characterised in that including：Tank body, the heating plate in tank body and the oil inlet pipe installed in heating plate one end, the heating plate includes a heating surface, the heating surface with respect to the horizontal plane has certain gradient, the oil inlet pipe is arranged on the slightly higher one end of the heating surface, and above the heating surface, some oil outlets are provided with the section that the oil inlet pipe is located on heating surface.
2. light hydrocarbon reactor according to claim 1, it is characterised in that the reactor includes polylith heating plate, the heating plate is placed in stacking.
3. light hydrocarbon reactor according to claim 2, it is characterised in that every piece of heating plate correspondence installs an oil inlet pipe.
4. light hydrocarbon reactor according to claim 1, it is characterised in that the inclination range of the heating surface is to be less than or equal to 45 ° more than 0 °.
5. light hydrocarbon reactor according to claim 1, it is characterised in that the tank body is cuboid or cylinder or other shapes for having an inner chamber.
6. light hydrocarbon reactor according to claim 1, it is characterised in that the tank body is the tank body of the hemispherical inner chamber in left and right ends.
7. light hydrocarbon reactor according to claim 6, it is characterised in that the reactor also includes air inlet pipe, the air inlet pipe is located at the heating plate top or bottom.
8. light hydrocarbon reactor according to claim 1, it is characterised in that the heating plate includes having heating medium in internal cavities, the internal cavities.
9. light hydrocarbon reactor according to claim 1, it is characterised in that heating plate upper surface temperature is more than 36 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510911961.2A CN107008212A (en) | 2016-01-28 | 2016-01-28 | Light hydrocarbon reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510911961.2A CN107008212A (en) | 2016-01-28 | 2016-01-28 | Light hydrocarbon reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107008212A true CN107008212A (en) | 2017-08-04 |
Family
ID=59438820
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510911961.2A Pending CN107008212A (en) | 2016-01-28 | 2016-01-28 | Light hydrocarbon reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107008212A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2380811Y (en) * | 1999-07-20 | 2000-05-31 | 宋雨 | Liquid-fuel gasifying apparatus |
| CN2436812Y (en) * | 1999-08-14 | 2001-06-27 | 兰州金福乐食品有限公司 | Evaporation type liquid fuel combustion gasifier |
| CN204911812U (en) * | 2015-07-28 | 2015-12-30 | 山西中煤华晋能源有限责任公司 | Flotation reagent's gasification equipment |
| CN106925184A (en) * | 2015-12-29 | 2017-07-07 | 常熟鼎天赫机械有限公司 | There is system in lighter hydrocarbons air mixture |
-
2016
- 2016-01-28 CN CN201510911961.2A patent/CN107008212A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2380811Y (en) * | 1999-07-20 | 2000-05-31 | 宋雨 | Liquid-fuel gasifying apparatus |
| CN2436812Y (en) * | 1999-08-14 | 2001-06-27 | 兰州金福乐食品有限公司 | Evaporation type liquid fuel combustion gasifier |
| CN204911812U (en) * | 2015-07-28 | 2015-12-30 | 山西中煤华晋能源有限责任公司 | Flotation reagent's gasification equipment |
| CN106925184A (en) * | 2015-12-29 | 2017-07-07 | 常熟鼎天赫机械有限公司 | There is system in lighter hydrocarbons air mixture |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170804 |
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| RJ01 | Rejection of invention patent application after publication |