CN113831929A - Device suitable for microwave separation oil rock - Google Patents

Device suitable for microwave separation oil rock Download PDF

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Publication number
CN113831929A
CN113831929A CN202111048792.6A CN202111048792A CN113831929A CN 113831929 A CN113831929 A CN 113831929A CN 202111048792 A CN202111048792 A CN 202111048792A CN 113831929 A CN113831929 A CN 113831929A
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waveguide
oil
microwave
cracking kettle
kettle
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王曙光
宗卫刚
王耀光
唐挺
唐小琴
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Chengdu Oula Microwave Components Co ltd
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Chengdu Oula Microwave Components Co ltd
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Priority to CN202111048792.6A priority Critical patent/CN113831929A/en
Publication of CN113831929A publication Critical patent/CN113831929A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/002Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal in combination with oil conversion- or refining processes

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The invention discloses a device suitable for microwave oil rock separation, which comprises a feeding machine, a microwave generating device, a cracking kettle, a waveguide and a discharging machine, wherein the microwave generating device is arranged on the feeding machine; the microwave generating device is connected with the waveguide which is connected with the cracking kettle; the microwave generating device is connected with a bent waveguide, the bent waveguide is connected with a circulator, the circulator is connected with a water load and a coupler, the coupler is connected with a rectangular waveguide, and the rectangular waveguide is connected with a waveguide pressure window and a circular waveguide through a rectangular-circular transition waveguide; a stirring device is arranged on the cracking kettle; the cracking kettle is provided with a waveguide connecting pipe, microwaves enter the cracking kettle from the waveguide connecting pipe, a waveguide pressure window is arranged on the waveguide connecting pipe, and the circular waveguide is connected with the waveguide pressure window; the top of the cracking kettle is provided with a gas phase outlet, and the bottom of the cracking kettle is connected with a discharging machine. This device heats the oil petrography in the pyrolysis kettle, derives the pyrolysis kettle with oil, water, the oil petrography waste residue after the separation smoothly. The device ensures the safety and high efficiency of the microwave separation process in the production flow.

Description

Device suitable for microwave separation oil rock
Technical Field
The invention provides a device suitable for microwave oil-rock separation, which creates a safe and effective microwave treatment environment and avoids the conditions of microwave ignition and thermal runaway.
Background
The global oil shale resource is very rich, and the amount of the resources stored in the oil shale is about 10 trillion tons according to incomplete statistics and is 40 percent more than that of coal resources. The oil shale is distributed intensively and has great potential and favorable conditions as a succeed energy source. The united states is the world with the most abundant resources of oil shale worldwide, and the reserves of 4100 million tons account for about 70% or more of the worldwide reserves. According to the resource quantity, 476 hundred million tons in China are only second to the United states and are located in the second world, and 400 hundred million tons in Russia are located in the third world. Although oil shale resources are abundant, only north america worldwide has achieved large-scale commercial development of oil shale, and China is still in the early development stage of oil shale.
The method for extracting shale oil from oil shale widely used in China is a smoothing furnace which is started to be used in the second war period and a rotary kiln. The smoothie furnace is used for heating the oil shale to 500 ℃ by utilizing high-temperature air to obtain oil in the oil shale. The smooth furnace has two defects, namely, a small oil shale blocks an oil-gas channel of the smooth furnace, and oil in the small oil shale cannot be extracted; and the low oil gas recovery rate causes high oil refining cost and large equipment maintenance cost. Due to the brittleness of the oil shale, the oil shale is very easy to break into small blocks during the mining process. These small pieces of oil shale cannot be refined, wasting a lot of resources. The rotary kiln is a new device introduced from abroad, and can rotate to drive the oil shale in the kiln to turn over so as to timely recover oil gas into a pipeline without being blocked by small oil shale. However, after actual use, the rotary kiln is found to be incapable of claiming 90% of oil recovery rate, but about 65% of oil recovery rate, and one rotary kiln has two billion purchase, maintenance and maintenance costs, so that the rotary kiln cannot be popularized and used at all.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provides a device suitable for microwave separation of oil rocks. The oil rock is sent into a cracking kettle, and the separated oil, water and oil rock waste residue are smoothly led out of the cracking kettle.
The purpose of the invention is realized by the following technical scheme:
a device suitable for microwave separation of oil rocks comprises a feeding machine, a microwave generating device, a cracking kettle, a waveguide and a discharging machine; the outlet of the feeding machine is communicated with the inlet of the cracking kettle; the microwave generating device is connected with the waveguide which is connected with the cracking kettle; the microwave generating device is connected with a bent waveguide, the bent waveguide is connected with a circulator, the circulator is connected with a water load and a coupler, the coupler is connected with a rectangular waveguide, and the rectangular waveguide is connected with a waveguide pressure window and a circular waveguide through a rectangular-circular transition waveguide;
a stirring device is arranged on the cracking kettle and comprises a first motor, a coupler, a stirring rod and a helical blade; the first motor is arranged above the cracking kettle, and the stirring rod is connected with the first motor through a coupler; the helical blade is arranged on the stirring rod;
the cracking kettle is provided with a waveguide connecting pipe, microwaves enter the cracking kettle from the waveguide connecting pipe, a waveguide pressure window is arranged on the waveguide connecting pipe, the circular waveguide is connected with the waveguide pressure window, and the length of the circular waveguide connected with the waveguide pressure window is 80-400 mm; the top of the cracking kettle is provided with a gas phase outlet, and the bottom of the cracking kettle is connected with a discharging machine (an oxygen isolating discharging machine).
The thermal insulation layer is arranged outside the cracking kettle and is a thermal insulation and thermal insulation material, so that the external radiation of the temperature in the cracking kettle is blocked, and the heating efficiency is improved.
Preferably, a thermometer port is provided in the pyrolysis reactor, and the thermometer port is used for installing a thermometer.
As the preferred mode, set up nitrogen gas mouth D on the pyrolysis reactor, be provided with clean hole on the waveguide connecting pipe, clean hole and confession nitrogen device link to each other. The nitrogen can prevent the high-temperature oil gas from exploding.
Preferably, the gas phase outlet is connected to a condenser.
Preferably, the condenser is connected to the oil-water separator. The separated gas enters a condenser from a gas phase outlet, is liquefied into liquid and flows into an oil-water separator.
Preferably, the oil-water separator is connected to the water receiving tank and the oil receiving tank, respectively. The oil-water separator separates the water in the lower layer into a water receiving tank; the upper layer of oil separates into an oil receiving tank.
As the preferred mode, the condenser is connected with the vacuumizing device, the vacuumizing device comprises a connecting pipeline, a buffer tank and a vacuum pump, the connecting pipeline is connected to the condenser, and the connecting pipeline is connected with the buffer tank and the vacuum pump.
As preferred mode, the ejection of compact machine is the cooling of the ejection of compact machine that separates oxygen for reducing the temperature, through the ejection of compact machine cooling that has water cooling plant during the waste material ejection of compact, and the ejection of compact machine is a seal structure's container simultaneously, and is isolated with the outside air, prevents that oxygen from getting into and the waste material of high temperature and remaining oil-gas mixture from appearing burning and exploding. The solid rock remained in the cracking kettle is discharged into a movable ash box through a temperature-reducing and oxygen-isolating discharging machine and is transported away.
As a preferred mode, the temperature-reducing and oxygen-isolating discharging machine comprises a screw conveyer, an oxygen-isolating discharging motor and a nitrogen inlet, wherein a rotating shaft of the screw conveyer is connected with the oxygen-isolating discharging motor; the nitrogen inlet is connected with a nitrogen supply device; the screw conveyer is provided with a solid residue inlet, a solid residue outlet, a water inlet and a water outlet.
The invention has the beneficial effects that:
the device adopts a microwave cracking method to heat the oil rock in the cracking kettle. The oil rock is sent into a cracking kettle, and the separated oil, water and oil rock waste residue are smoothly led out of the cracking kettle. The device ensures the safety and high efficiency of the microwave separation process in the production flow. It can be widely used in mass production.
Drawings
In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings that are required to be used in the embodiments will be briefly described below, it should be understood that the following drawings only illustrate some embodiments of the present invention and therefore should not be considered as limiting the scope, and for those skilled in the art, other related drawings can be obtained according to the drawings without inventive efforts.
FIG. 1 is a schematic view of the apparatus of the present invention;
FIG. 2 is a second overall view of the apparatus of the present invention;
FIG. 3 is a schematic view of the structure of a cracking kettle;
FIG. 4 is one of the schematic structural diagrams at the waveguide connecting tube;
FIG. 5 is a second schematic view of the waveguide connecting tube;
FIG. 6 is a third schematic view of the waveguide connecting tube;
FIG. 7 is a top view of a cleavage kettle cover plate;
FIG. 8 is a schematic view of a labyrinth choke;
FIG. 9 is a schematic structural view of a shielding discharging machine;
in the figure, 1-an activated powder bin, 2-a feeder, 3-a steel platform, 4-a pyrolysis kettle, 5-a condensing device, 6-an oil-water separator, 7-a water receiving tank, 8-an oil receiving tank, 9-a vacuum pump, 10-a first microwave generator, 11-a straight waveguide, 12-a circulator, 13-a water load, 14-a coupler, 15-a three-screw tuner, 16-a square circle transition, 17-a waveguide pressure window, 18-an oxygen insulation discharging machine, 18.1-a nitrogen inlet, 18.2-a solid residue inlet, 18.3-a water inlet, 18.4-a screw conveyor, 18.5-a water outlet, 18.6-a solid residue outlet, 18.7-an oxygen insulation discharging motor, 19-a movable ash box, 20-a second microwave generator, 21-a labyrinth choke, 22-gas phase outlet, 23-waveguide connecting pipe, 23.1-pneumatic cleaning hole, 23.2-manual cleaning hole, 24-stirring rod, 25-helical blade, 26-outer layer, 27-inner layer, 28-cable, 29-power meter, 30-nitrogen tank, 31-nitrogen making machine, 32-buffer tank and 33-heat insulating layer.
Detailed Description
The technical solutions of the present invention are further described in detail below with reference to the accompanying drawings, but the scope of the present invention is not limited to the following.
In order to make the objects, technical solutions and advantages of the embodiments of the present invention more apparent, the technical solutions of the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings of the embodiments of the present invention, and it is obvious that the described embodiments are some, but not all embodiments of the present invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention. Thus, the following detailed description of the embodiments of the present invention, presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention.
In the description of the present invention, it is to be understood that the terms indicating an orientation or positional relationship are based on the orientation or positional relationship shown in the drawings only for the convenience of describing the present invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention.
In the present invention, unless otherwise specifically stated or limited, the terms "mounted," "connected," and "fixed" should be construed broadly and include, for example, fixed connections, detachable connections, or integral parts; can be mechanically or electrically connected; either directly or indirectly through intervening media, either internally or in any other relationship. The specific meanings of the above terms in the present invention can be understood by those skilled in the art according to specific situations.
In the present invention, unless otherwise expressly stated or limited, the presence of a first feature above or below a second feature may encompass both the first and second features being in direct contact, and also may encompass both the first and second features being in contact, not being in direct contact, but rather being in contact with another feature therebetween. Also, the first feature being above, on or above the second feature includes the first feature being directly above and obliquely above the second feature, or merely means that the first feature is at a higher level than the second feature. Including a first feature being directly below and obliquely below a second feature, or simply indicating that the first feature is at a lesser elevation than the second feature, if present below, under or below the second feature.
Example one
As shown in fig. 1, a device suitable for microwave oil-rock separation comprises a feeding machine 2, a microwave generating device, a cracking kettle 4, a waveguide and a discharging machine; the outlet of the feeding machine 2 is communicated with the inlet of the cracking kettle 4, the microwave generating device is connected with the waveguide, and the waveguide is connected with the cracking kettle 4.
A stirring device is arranged on the cracking kettle 4, and comprises a first motor, a coupler, a stirring rod 22 and a helical blade 23; the first motor is arranged above the cracking kettle 4, and the stirring rod 22 is connected with the first motor through a coupler; the helical blade 23 is arranged on the stirring rod 22;
the cracking kettle 4 is provided with a waveguide connecting pipe 23, the microwave enters the cracking kettle 4 from the waveguide connecting pipe 23, and the waveguide length of the waveguide connecting pipe 23 is 80-400 mm.
When high power microwave is fed into the cracking kettle 4, the waveguide length is limited by the microwave transmission characteristic, when the waveguide length is less than 1/4 waveguide wavelength, the microwave can be cut off, and oilstone dust in the cracking kettle 4 with too short length can enter the waveguide connecting pipe 23 under the stirring condition, so that the normal feeding of the microwave is influenced, and the waveguide length of the waveguide connecting pipe 23 is 80-400 mm.
The waveguide is provided with a waveguide pressure window 17 (the waveguide pressure window 17 is additionally arranged on the waveguide connecting pipe 23 to realize electromagnetic sealing and vacuum sealing)
The top of the cracking kettle 4 is provided with a gas phase outlet 22, and the bottom of the cracking kettle 4 is connected with a discharging machine.
This embodiment is through feeding in the microwave in the wave guide pyrolysis cauldron 4, heats the oil petrography, and the oil petrography begins the schizolysis to separate out oil gas when the temperature reaches 100 ~ 450 ℃.
Example two
In order to monitor the temperature in the cracking kettle 4 in real time, in this embodiment, a thermometer port (see T1 in fig. 7) is disposed on a cover plate of the cracking kettle 4, the thermometer port is used for installing a thermometer, the thermometer monitors the temperature of the oil in the cracking kettle, a thermometer port T2 (see T2 in fig. 3) is disposed in the middle section of the kettle body, and the thermometer is installed in the middle section of the kettle body to monitor the temperature of the oil and rock material in the cracking kettle 4, so as to adjust the microwave input power in time.
The thermal insulation layer 33 is arranged outside the cracking kettle 4, the thermal insulation layer 33 is a thermal insulation and heat insulation material, the external radiation of the temperature in the cracking kettle 4 is blocked, and the heating efficiency is improved.
Further, a vacuum pressure gauge port P is also arranged on the cover plate of the cracking kettle 4. The pressure gauge is used for detecting the vacuum degree in the cracking kettle 4 and ensuring the low-pressure and low-oxygen cracking environment.
EXAMPLE III
The cracking kettle 4 is provided with a nitrogen port D, and the nitrogen port D is connected with a nitrogen supply device (such as a nitrogen generator 31). A nitrogen port (a pneumatic cleaning hole 23.1) is arranged on the waveguide close to the waveguide pressure window 17, and after the oil rock material is fed, nitrogen is started to flush the waveguide pressure window 17, so that dust and oil gas are prevented from polluting the waveguide pressure window 17.
Further, a cleaning hole is provided on the waveguide connection pipe 23. As shown in fig. 3-6, the cleaning holes include a manual cleaning hole 23.2 and a pneumatic cleaning hole 23.1. The manual cleaning hole 23.2 is arranged on a straight pipe which is communicated with the waveguide connecting pipe 23. The manual cleaning aperture 23.2 is opened at a distance of 27-30cm from the waveguide pressure window 17.
The pneumatic cleaning hole 23.1 is arranged on an air inlet device, and the air inlet device comprises a short pipe, an arc pipe and two branch pipes; the arc-shaped pipe is respectively connected with the short pipe and the two branch pipes. The two branch pipes are arranged on the outer wall of the waveguide connecting pipe 23 in an angle of 180 degrees. The pneumatic cleaning hole 23.1 is arranged on the opposite side of the manual cleaning hole 23.2.
A manual cleaning hole 23.2 and a pneumatic cleaning hole 23.1 are provided on the waveguide connection pipe 23. When materials are stirred, although a certain waveguide length is set to prevent the materials from splashing on the waveguide pressure window 17, in actual production, part of the materials cannot be prevented from splashing to pollute the waveguide pressure window 17, and then microwave ignition is caused, so that the waveguide pressure window 17 is manually and pneumatically cleaned to form the hole 23.1. From which manual cleaning or pneumatic cleaning can be initiated when there is a foreign object on the waveguide pressure window 17.
Example four
For the treatment of gaseous oil, the gas phase outlet 22 (see N4 in fig. 7) of this embodiment is connected to a condenser (condensing unit 5 shown in fig. 1). The condenser is connected with the oil-water separator 6. As shown in fig. 3, the separated gas enters the condenser from the gas phase outlet 22N4, and is liquefied into a liquid state and flows into the oil-water separator 6.
As shown in fig. 1 and 2, the oil-water separator 6 is connected to a water receiving tank 7 and an oil receiving tank 8, respectively. The oil-water separator 6 separates the water in the lower layer into a water receiving tank 7; the upper layer of oil separates into an oil receiving tank 8.
EXAMPLE five
The discharging machine is a temperature-reducing oxygen-isolating discharging machine 18. The solid residue remained in the cracking kettle 4 is discharged to a movable ash residue box 19 through a temperature-reducing oxygen-isolating discharging machine 18 and is transported away. The temperature-reducing and oxygen-isolating discharging machine 18 comprises a screw conveyer 18.4, an oxygen-isolating discharging motor 18.7 and a nitrogen inlet 18.1, wherein a rotating shaft of the screw conveyer 18.4 is connected with the oxygen-isolating discharging motor 18.7; the nitrogen inlet 18.1 is connected with a nitrogen supply device; the screw conveyer 18.4 is provided with a solid residue inlet 18.2, a solid residue outlet 18.6, a water inlet 18.3 and a water outlet 18.5. The discharging machine with the water cooling device is used for cooling during discharging of waste materials, and the discharging machine is a container with a sealing structure and isolated from outside air, so that oxygen is prevented from entering the waste materials with high temperature and burning explosion of residual oil-gas mixture is prevented.
As shown in fig. 9, the solid residue inlet 18.2 is arranged at the top of one side of the screw conveyor 18.4, and the solid residue outlet 18.6 is arranged at the bottom of the other side of the screw conveyor 18.4. The water inlet 18.3 is arranged at the bottom of one side of the screw conveyer 18.4, and the water outlet 18.5 is arranged at the top of the other side of the screw conveyer 18.4. The solid residue inlet 18.2 and the water inlet 18.3 are located on the same side of the screw conveyor 18.4. The solid residue outlet 18.6 and the water outlet 18.5 are positioned at the same side of the screw conveyor 18.4. A nitrogen inlet 18.1 is provided at the end of the screw conveyor 18.4 near the solid residue inlet 18.2 or the water inlet 18.3. The oxygen-isolating discharging motor 18.7 is arranged at the other end of the screw conveyer 18.4 and is close to the solid residue outlet 18.6 and the water outlet 18.5.
When the residual solid residue is discharged from the cracking kettle 4, the temperature is very high just after microwave heating, so that once the residual solid residue is contacted with air, the risk of deflagration exists, and the residual high-temperature solid residue needs to be cooled and discharged in an oxygen-isolating way by using a cooling and oxygen-isolating discharging machine 18.
EXAMPLE six
To improve power capacity, circular waveguide transmission is used. Circular waveguides have a greater power capability than rectangular waveguides. Rectangular waveguide output by the microwave generating device is converted into circular waveguide by a rectangular-circular transition 16 waveguide to be injected into the cracking kettle 4.
A vacuumizing device (comprising a buffer tank 32 and a vacuum pump 9) is connected between the condenser and the oil-water separator 6, the vacuumizing device comprises a connecting pipeline, the buffer tank 32 and the vacuum pump 9, the connecting pipeline is connected to the condensing device 5, and the connecting pipeline is connected with the buffer tank 32 and the vacuum pump 9.
EXAMPLE seven
The two feed waveguides N1, N2 may back up each other, and when one feed waveguide fails, the other feed waveguide may be activated without affecting the operation. As shown in fig. 1 and 2, two feeding waveguides N1 and N2 are respectively connected to two microwave generators (including a microwave generator and a power supply). The first microwave generator 10 is connected to an angled waveguide, which is connected to a circulator 12, the circulator 12 is connected to a coupler 14, the coupler 14 is connected to a rectangular waveguide, which is connected to a circular waveguide via a rectangular-circular transition 16 waveguide, which extends into a feed waveguide N1. The second microwave generator 20 is connected to an elbow waveguide, which is connected to the circulator 12, the circulator 12 is connected to the coupler 14, the coupler 14 is connected to a rectangular waveguide (the straight waveguide 11 shown in fig. 1), which is connected to a circular waveguide by a rectangular-circular transition 16 waveguide, which extends into the feed waveguide N2. Three screw adapters 15 are provided on the rectangular waveguide.
Further, the circulator 12 is also connected to a water load 13, and the water load 13 can absorb the reflected power from the cracking kettle and play a role in protecting the microwave source (microwave generator).
The circulator 12 is a one-way device for microwave transmission, and when used together with the water load 13, the reflected power generated in the cracking kettle 4 can be transmitted to the water load 13, the water load 13 converts the reflected power into heat after absorption and dissipates the heat, and the reflected power is prevented from being transmitted to a microwave source (microwave generator) to influence the stable use of the microwave source.
The coupler 14 can couple out small power below 100mw in a high-power microwave environment for detecting the magnitude of microwave power and whether power transmission is normal. The coupler 14 is connected to a power meter 29 through a cable 28 (coaxial cable), and the power meter 29 is used for displaying specific power values.
The straight waveguide 11 and the bent waveguide are devices for conducting microwave power, which is conducted from a microwave source to the cracker 4 and fed.
The reflected power generated in the cracker kettle 4 will reduce the efficiency of the cracker kettle 4, and at the same time, the reflected microwave power will interfere with the stable operation and service life of the microwave source, and the three-pin coordinator 15 can adjust the reflected power within a certain range to keep the reflected power at the lowest possible level.
The waveguide pressure window 17 is a sealed device made of microwave-transparent material, which can isolate the air flow and does not affect the microwave power passing.
The transition waveguide (rectangular-circular transition 16) converts a rectangular waveguide into a circular waveguide, allowing more uniform microwave power feed to the cracker 4.
Example eight
In order to prevent the microwave leakage from causing electromagnetic radiation damage to the environment, electromagnetic shielding is needed to the cracking kettle 4, and the invention adopts a labyrinth choke 21 to shield the microwave leakage. As shown in fig. 1, at the cracking kettle 4b (i.e. the intersection connection part of the lid of the cracking kettle 4, the stirring shaft and the labyrinth choke), which is a weak link of the whole cracking kettle 4, the microwave will converge at the b position when reflected in the cracking kettle 4, and the high-intensity microwave will break down the b position, so that a microwave dynamic sealing device, i.e. the labyrinth choke 21, is required at the b position to protect the weak link.
The labyrinth choke 21 is constructed as shown in fig. 8, and the labyrinth gap corresponds to a radiation resistance. External electromagnetic field with close frequency can excite current in the choke through the radiation resistor; so that the input impedance of the outer layer (see fig. 8) is connected in series to a point near λ/4 of the inner layer; but Z isinAbout 0, so that the current flows through this Z on the slotin(ZinInput impedance) becomes smaller order of magnitude, greatly suppresses leakage power, realizes the effect of choking, and thenThereby realizing electromagnetic sealing. The weak link b can be protected by adopting the design, and microwave ignition is avoided.
Example nine
To prevent the edge of the stirring rod 24 from sparking, the edge of the helical blade 25 of the stirring rod 24 is smoothly rounded. 24 helical blade 25 of stirring rod has set up 25 mm's distance to 4 walls of pyrolysis kettle, prevents that stirring rod 24 from touching 4 inner walls of pyrolysis kettle stirring rod 24 blocks. The stirring rod 24 and the helical blade 25 can turn the oil rock 1-2 times from bottom to top in one minute.
Example ten
The top of the cracking kettle 4 is provided with an air extraction opening which is connected with a condenser and a vacuum pump 9.
The vacuum pump 9 pumps out the air in the cracking kettle 4 to keep the air pressure in the cracking kettle 4 between-0.09 MPa and-0.097 MPa. Under the action of negative pressure pumping, the volatilized oil gas is guided to enter a condenser for condensation and separation; secondly, isolating oxygen in the cracking kettle 4 to prevent oil gas from being oxidized; and thirdly, preventing the oil gas from being combusted and exploded in microwave and high-temperature environments. The material is fully stirred by the stirring rod 24, which is beneficial to uniformly heating the material by microwave.
The embodiment further comprises a nitrogen generator 31, and the nitrogen generator 31 generates nitrogen gas. The nitrogen tank 30 is connected with the nitrogen generator 31, and the nitrogen tank 30 is used for storing nitrogen.
EXAMPLE eleven
The feeding machine 2 is connected with the activating powder bin 1, and the feeding machine 2 is a spiral conveying device. The activated powder is the crushed oil rock.
Example twelve
Cracking kettle 4 sets up on steel platform 3, the operation of being convenient for on the one hand, and on the other hand cracking kettle 4 has certain height, the ejection of compact of being convenient for.
A movable ash box 19 is arranged below the cracking kettle 4.
While preferred embodiments of the present invention have been described, additional variations and modifications in those embodiments may occur to those skilled in the art once they learn of the basic inventive concepts. Therefore, it is intended that the appended claims be interpreted as including preferred embodiments and all such alterations and modifications as fall within the scope of the invention. The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the invention, it should be noted that any modifications, equivalents and improvements made within the spirit and principle of the present invention should be included in the scope of the present invention.

Claims (9)

1. The utility model provides a device suitable for microwave separation oil rock which characterized in that: comprises a feeding machine, a microwave generating device, a cracking kettle, a waveguide and a discharging machine; the outlet of the feeding machine is communicated with the inlet of the cracking kettle; the microwave generating device is connected with the waveguide which is connected with the cracking kettle; the microwave generating device is connected with a bent waveguide, the bent waveguide is connected with a circulator, the circulator is connected with a water load and a coupler, the coupler is connected with a rectangular waveguide, and the rectangular waveguide is connected with a waveguide pressure window and a circular waveguide through a rectangular-circular transition waveguide;
a stirring device is arranged on the cracking kettle and comprises a first motor, a coupler, a stirring rod and a helical blade; the first motor is arranged above the cracking kettle, and the stirring rod is connected with the first motor through a coupler; the helical blade is arranged on the stirring rod;
the cracking kettle is provided with a waveguide connecting pipe, microwaves enter the cracking kettle from the waveguide connecting pipe, a waveguide pressure window is arranged on the waveguide connecting pipe, the circular waveguide is connected with the waveguide pressure window, and the length of the circular waveguide connected with the waveguide pressure window is 80-400 mm; the top of the cracking kettle is provided with a gas phase outlet, and the bottom of the cracking kettle is connected with a discharging machine.
2. The device for microwave separation of oil rocks according to claim 1, characterized in that: a thermometer port is arranged on the cracking kettle and used for installing a thermometer.
3. The device for microwave separation of oil rocks according to claim 1, characterized in that: a nitrogen port D is arranged on the cracking kettle, and a cleaning hole is arranged on the waveguide connecting pipe and connected with a nitrogen supply device.
4. The device for microwave separation of oil rocks according to claim 1, characterized in that: the gas phase outlet is connected with a condenser.
5. An apparatus suitable for microwave separation of oil rocks according to claim 4, characterized in that: the condenser is connected with the oil-water separator.
6. An apparatus suitable for microwave separation of oil rocks according to claim 5, characterized in that: the oil-water separator is respectively connected with the water receiving tank and the oil receiving tank.
7. An apparatus suitable for microwave separation of oil rocks according to claim 5, characterized in that: the condenser is connected with the vacuumizing device, the vacuumizing device comprises a connecting pipeline, a buffer tank and a vacuum pump, the connecting pipeline is connected to the condenser, and the connecting pipeline is connected with the buffer tank and the vacuum pump.
8. The device for microwave separation of oil rocks according to claim 1, characterized in that: the discharging machine is a temperature-reducing oxygen-isolating discharging machine.
9. An apparatus suitable for microwave separation of oil rocks according to claim 8, characterized in that: the temperature-reducing and oxygen-isolating discharging machine comprises a screw conveyer, an oxygen-isolating discharging motor and a nitrogen inlet, and a rotating shaft of the screw conveyer is connected with the oxygen-isolating discharging motor; the nitrogen inlet is connected with a nitrogen supply device; the screw conveyer is provided with a solid residue inlet, a solid residue outlet, a water inlet and a water outlet.
CN202111048792.6A 2021-09-08 2021-09-08 Device suitable for microwave separation oil rock Pending CN113831929A (en)

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