CN208632464U - A kind of generating device for light hydrocarbon oil-gas separation - Google Patents

Abstract

It is a kind of to be related to a kind of generating device applied to light hydrocarbon oil-gas separation in liquid fuel gasification field, comprising tank body, intake stack and heating device occurs；The upper half that tank body occurs is equipped with oil inlet, gas outlet and air inlet, and the bottom that tank body occurs is equipped with sewage draining exit；One end of the intake stack is connect with air supply device, its other end is seamless to pass through connection corresponding with bellows chamber after air inlet, bellows chamber is corresponding to be located at the center that the tank inner chamber upper half occurs, bellows chamber bottom is uniformly communicated at least three blowing lines, and the nozzle of blowing line is corresponding to be located at the intracorporal bottom of generation tank；The heating device is located at the lower half that tank inner chamber occurs；It can satisfy the demand for preparing a large amount of light-hydrocarbon gas, and preparation efficiency is high.

Description

A kind of generating device for light hydrocarbon oil-gas separation

Technical field

The utility model relates to lighter hydrocarbons application fields, fill more particularly, to a kind of applied to light hydrocarbon oil-gas separation It sets.

Background technique

Well known, demand of the mankind to the energy increasingly increases with the rapid development of society, and fossil fuel is used as to be made at present With one of most commonly used energy, the speed of consumption is far beyond the reproduction speed of nature, in addition, fossil fuel Directly burn also very big to the harm of environment, be one of the arch-criminal for causing global warming and atmosphere pollution, therefore, people couple Using and developing for green energy resource is also just increasingly paid attention to；Traditional lighter hydrocarbons oil liquid generating device is to be made of Bubbling method gently Hydrocarbon combustion gas utilizes light-hydrocarbon gas made of this method since party's legal system light-hydrocarbon gas is completed in bubbling reactor Amount is directly proportional to the volume of bubbling reactor, if user is larger to the demand of light-hydrocarbon gas, needs to cooperate more great Rong Long-pending bubbling reactor prepares light-hydrocarbon gas, and because the technique that requires in production of the bubbling reactor of big volume is higher, So existing bubbling reactor volume is less than normal, thus it is less using the amount that this method prepares gas, cause a large amount of in preparation Light-hydrocarbon gas when its gas processed higher cost；

Chinese patent (CN00233226.4) discloses a kind of lighter hydrocarbons oil liquid gasification installation, which utilizes bubbling Device heats liquid light hydrocarbon by electric constant-temp device to prepare light-hydrocarbon gas, and liquid light hydrocarbon and air is promoted to contact It can gasify rapidly later, although which can be realized to gasify liquid light hydrocarbon is prepared into light-hydrocarbon gas, but the patent Structure it is complex and larger to energy consumption, so that production cost is higher.

Summary of the invention

In order to overcome the shortcomings in the background art, the utility model discloses can effectively solve the problem that propose in background technique A kind of lighter hydrocarbons oil liquid generating device of problem.

For achieving the above object, the utility model adopts the following technical solution:

A kind of generating device applied to light hydrocarbon oil-gas separation, comprising tank body, intake stack and heating device occurs；It is described The upper half that tank body occurs is equipped with oil inlet, gas outlet and air inlet, and the bottom that tank body occurs is equipped with sewage draining exit；The blast pipe The one end in road is connect with air supply device, and the other end is seamless to pass through connection corresponding with bellows chamber after air inlet, and bellows chamber is corresponding to be located at hair The center of the raw tank inner chamber upper half, bellows chamber bottom is uniformly communicated at least three blowing lines, the blowing line Nozzle far from bellows chamber one end is corresponding to be located at the intracorporal bottom position of generation tank；The heating device is located in generation tank body The lower half of chamber.

Further, the heating device is the heating coil that inside is passed through thermal medium.

Further, the both ends nozzle of the heating coil is connected after extending to generation tank body outside by circulating-heating pump It is logical, form circulation loop, and the corresponding top for being located at entrance in outlet of heating coil.

Further, the thermal medium is hot water or hot coal oil.

Further, the distance of the gas outlet to generation tank body top surface is gas outlet to generation tank body bottom faces distance One third.

Further, the nozzle that the blowing line is located at the intracorporal bottom of generation tank is equipped with filter screen.

Further, the mesh number of the filter screen is 80-120 mesh.

Further, the generation top of the tank is equipped with pressure sensor and auto-manual exhaust valve.

Further, the generation tank body is equipped with temperature sensor.

Further, the generation tank body is equipped with liquid level sensor and liquid level display.

Due to the adoption of the technical scheme as described above, the utility model has the following beneficial effects:

Lighter hydrocarbons oil liquid generating device described in the utility model, the lighter hydrocarbons oil liquid first in petroleum tank are entered by oil inlet Occur in tank body, the lighter hydrocarbons oil liquid occurred in tank body is heated by heating device later, when lighter hydrocarbons oil liquid is heated to centainly After temperature, lighter hydrocarbons oil liquid, which passes through, can be generated a certain amount of light hydrocarbon oil-gas by thermal decomposition, and air supply device starts to intake stack at this time It is blown into air, air can be divided by blowing line set by bellows chamber by multichannel, multichannel air is blown from blowing line later Out, air can carry light hydrocarbon oil-gas during rising and rise together, and the mixed gas of final light hydrocarbon oil-gas and air is logical It crosses gas outlet and enters next process；The heating device of the lower half for being located at generation tank inner chamber can be to lighter hydrocarbons oil liquid The circulation loop for being evenly heated, and being formed by circulating-heating pump and heating coil, additionally it is possible to keep thermal medium In certain temperature range；In addition, the generation tank body can also pass through the pressure sensor, temperature sensor and liquid of setting Face sensor reaches real-time detection and pressure in tank body, the height of the temperature of lighter hydrocarbons oil liquid and lighter hydrocarbons oil liquid liquid level occurs Purpose ensures that operation safety when light hydrocarbon oil-gas separates in generation tank body.

Detailed description of the invention

Fig. 1 is the structural schematic diagram of the utility model；

In figure: 1, tank body occurs；2, intake stack；3, bellows chamber；4, blowing line；5, heating device；6, gas outlet；7, it presses Force snesor；8, temperature sensor；9, liquid level sensor；10, sewage draining exit.

Specific embodiment

The present invention can be explained in more detail by the following examples, open the purpose of this utility model is intended to protect this All changes and improvements within the scope of utility model, the utility model are not limited by the following examples:

In conjunction with attached drawing 1, the lighter hydrocarbons oil liquid generating device, comprising tank body 1, intake stack 2 and heating device 5 occurs； The top that tank body 1 occurs is respectively equipped with oil inlet, gas outlet 6 and air inlet, in addition, under the same conditions, by multiple Test obtains, and the lighter hydrocarbons oil liquid in petroleum tank is entered by oil inlet to be occurred in tank body 1, when the liquid level of lighter hydrocarbons oil liquid is hair The half of raw 1 height of tank body, and gas outlet 6 is arrived for gas outlet 6 to the distance that 1 top surface of tank body occurs and 1 bottom of tank body occurs Portion's identity distance from one third when, the preparation efficiency of light-hydrocarbon gas can reach most preferably, it is described occur tank body 1 bottom be equipped with row Dirty mouth 10 can will occur the lighter hydrocarbons oil liquid residue in tank body 1 and generation tank is discharged；One end of the intake stack 2 and air feed fill Connection is set, the other end is seamless to pass through connection corresponding with bellows chamber 3 after air inlet, and bellows chamber 3 is corresponding to be located at generation 1 inner cavity upper half of tank body The center in portion, and 3 bottom of bellows chamber is uniformly communicated at least three blowing lines 4, and all blowing lines 4 are far from bellows chamber 3 The nozzle of one end is corresponding to pass through wind after air supply device is blown into air to intake stack 2 close to the interior bottom faces that tank body 1 occurs Air is divided into multichannel by blowing line 4 set by packet 3, and multichannel air is blown out from blowing line 4 later, then again along generation tank Bottom faces and inner wall dispersion rise in body 1, and air can carry the light of the heated rear generation of lighter hydrocarbons oil liquid during rising Hydrocarbon ils gas；In addition, blowing line 4 is equipped with corresponding filter screen far from the nozzle of 3 one end of bellows chamber, the mesh of filter screen can be utilized The air for blowing out blowing line 4 more disperses, to increase the contact area of air Yu lighter hydrocarbons oil liquid, air can be carried More light hydrocarbon oil-gas, as needed, the mesh number of the filter screen are set as 80-120 mesh；

The heating device 5 is located at the lower half that 1 inner cavity of tank body occurs, in addition, heating device 5 is that inside has been passed through heat The heating coil of medium can be evenly heated lighter hydrocarbons oil liquid, and lighter hydrocarbons oil liquid is a certain amount of by that can be generated by thermal decomposition Light hydrocarbon oil-gas, and the both ends nozzle of heating coil is extended to by circulating-heating pump connection after 1 outside of tank body occurs, and formation follows Loop back path, and the corresponding top for being located at entrance in outlet of heating coil, enable thermal medium to heat by circulating-heating pump, from And by certain temperature range that is maintained at of thermal medium, and thermal medium can follow between heating coil and circulating-heating pump Circulation is dynamic, and as needed, the thermal medium is set as hot water or hot coal oil；It is used in addition, being equipped at the top of the generation tank body 1 The pressure sensor 7 of 1 inner cavity air pressure of tank body, and matched auto-manual exhaust corresponding with pressure sensor 7 occurs in detection Valve, thus pressure information in the tank that auto-manual exhaust valve can either be made to be fed back according to pressure sensor 7, automatic implementation will occur Operation of the pressure control at 0.6 ± 0.1 kilogram in tank body 1, additionally it is possible to by user manually to auto-manual exhaust valve into Row switch operation, realizes that the purpose of air pressure in tank body 1 occurs for control；Tank body 1 occurs to be equipped with for detecting lighter hydrocarbons oil liquid temperature in tank The temperature sensor 8 of degree, so as to the temperature information of lighter hydrocarbons oil liquid in the tank that is fed back according to temperature sensor 8, come implement by Operation of the temperature control of lighter hydrocarbons oil liquid at 18-30 ° in tank；Tank body 1 occurs to be additionally provided with for detecting lighter hydrocarbons oil in generation tank body 1 The liquid level sensor 9 of liquid liquid level, and matched liquid level display corresponding with liquid level sensor 9, when the liquid level of lighter hydrocarbons oil liquid is high Degree is more than when the half of 1 height of tank body occurs, and liquid level sensor 9 can carry out warning reminding, and user in time , manually to injection oil liquid or discharge oil liquid in tank body 1 occurs, it can make to send out according to the liquid level shown by liquid level display The liquid level of raw 1 inner fluid of tank body is maintained at the half that 1 height of tank body occurs.

When implementing light-hydrocarbon fuel generating device described in the utility model, the lighter hydrocarbons oil liquid first in petroleum tank passes through oil inlet Mouth, which enters, to be occurred later to heat lighter hydrocarbons oil liquid by heating device 5, in tank body 1 when lighter hydrocarbons oil liquid is heated to certain temperature Afterwards, air supply device starts to be blown into air to intake stack 2, leads to after air is divided into multichannel by blowing line 4 set by bellows chamber 3 Enter in lighter hydrocarbons oil liquid, air can be carried during rising lighter hydrocarbons oil liquid generation light hydrocarbon oil-gas, final light hydrocarbon oil-gas with The mixed gas of air enters next process by gas outlet 6.

The non-detailed portion of the utility model is the prior art, therefore the utility model is not described in detail.

Claims (10)

1. it is a kind of applied to light hydrocarbon oil-gas separation generating device, it is characterized in that: comprising occur tank body (1), intake stack (2) and Heating device (5)；The upper half that tank body (1) occurs is equipped with oil inlet, gas outlet (6) and air inlet, and tank body (1) occurs Bottom is equipped with sewage draining exit (10)；One end of the intake stack (2) is connect with air supply device, and the other end is seamless to pass through air inlet Connection corresponding with bellows chamber (3) afterwards, bellows chamber (3) is corresponding to be located at the center that tank body (1) inner cavity upper half occurs, bellows chamber (3) bottom Portion is uniformly communicated at least three blowing lines (4), and the nozzle of blowing line (4) is corresponding to be located at the bottom occurred in tank body (1) Portion；The heating device (5) is located at the lower half that tank body (1) inner cavity occurs.

2. generating device according to claim 1, it is characterized in that: the heating device (5) is that inside has been passed through heating agent The heating coil of medium.

3. generating device according to claim 2, it is characterized in that: the both ends nozzle of the heating coil extends to generation It is connected to behind tank body (1) outside by circulating-heating pump, forms circulation loop, and the outlet of heating coil is corresponding positioned at the upper of entrance Side.

4. generating device according to claim 2, it is characterized in that: the thermal medium is hot water or hot coal oil.

5. generating device according to claim 1, it is characterized in that: the gas outlet (6), which is arrived, occurs tank body (1) top surface Distance be gas outlet (6) to occur tank body (1) bottom faces distance one third.

6. generating device according to claim 1, it is characterized in that: the nozzle of the blowing line (4) is correspondingly provided with filtering Net.

7. generating device according to claim 6, it is characterized in that: the mesh number of the filter screen is 80-120 mesh.

8. generating device according to claim 1, it is characterized in that: being equipped with pressure sensing at the top of the generation tank body (1) Device (7) and auto-manual exhaust valve.

9. generating device according to claim 1, it is characterized in that: the generation tank body (1) is equipped with temperature sensor (8).

10. generating device according to claim 1, it is characterized in that: the generation tank body (1) is equipped with liquid level sensor (9) and liquid level display.