CN207596787U - Oil smoke extraction regeneration oil product equipment in organic carbon - Google Patents
Oil smoke extraction regeneration oil product equipment in organic carbon Download PDFInfo
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- CN207596787U CN207596787U CN201721355316.8U CN201721355316U CN207596787U CN 207596787 U CN207596787 U CN 207596787U CN 201721355316 U CN201721355316 U CN 201721355316U CN 207596787 U CN207596787 U CN 207596787U
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- oil
- water
- pipe
- tank
- miscella
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- 239000000779 smoke Substances 0.000 title claims abstract description 32
- 230000008929 regeneration Effects 0.000 title claims abstract description 24
- 238000011069 regeneration method Methods 0.000 title claims abstract description 24
- 238000000605 extraction Methods 0.000 title claims abstract description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 16
- 229910052799 carbon Inorganic materials 0.000 title claims abstract description 16
- 239000007789 gas Substances 0.000 claims abstract description 66
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 65
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 38
- 239000003546 flue gas Substances 0.000 claims abstract description 38
- 238000010521 absorption reaction Methods 0.000 claims abstract description 16
- 238000005086 pumping Methods 0.000 claims abstract description 3
- 239000002904 solvent Substances 0.000 claims description 48
- 238000001816 cooling Methods 0.000 claims description 40
- 239000000945 filler Substances 0.000 claims description 22
- 239000003129 oil well Substances 0.000 claims description 22
- 239000007790 solid phase Substances 0.000 claims description 20
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 19
- 239000000919 ceramic Substances 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 4
- 238000003860 storage Methods 0.000 claims description 3
- 235000019504 cigarettes Nutrition 0.000 claims 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 14
- 238000004519 manufacturing process Methods 0.000 abstract description 7
- 238000002156 mixing Methods 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 4
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000004523 catalytic cracking Methods 0.000 abstract description 3
- 125000004122 cyclic group Chemical group 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 3
- 239000004615 ingredient Substances 0.000 abstract description 3
- 239000002737 fuel gas Substances 0.000 abstract description 2
- 235000019198 oils Nutrition 0.000 description 124
- 230000008859 change Effects 0.000 description 7
- 230000008676 import Effects 0.000 description 7
- 239000007788 liquid Substances 0.000 description 7
- 239000004215 Carbon black (E152) Substances 0.000 description 6
- 229930195733 hydrocarbon Natural products 0.000 description 6
- 150000002430 hydrocarbons Chemical class 0.000 description 6
- 239000005416 organic matter Substances 0.000 description 5
- 239000012071 phase Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- -1 and when initial Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000011449 brick Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 235000019476 oil-water mixture Nutrition 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005474 detonation Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- MEKDPHXPVMKCON-UHFFFAOYSA-N ethane;methane Chemical compound C.CC MEKDPHXPVMKCON-UHFFFAOYSA-N 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- CSJDCSCTVDEHRN-UHFFFAOYSA-N methane;molecular oxygen Chemical compound C.O=O CSJDCSCTVDEHRN-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 150000002927 oxygen compounds Chemical class 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 239000002341 toxic gas Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model discloses the oil smoke extraction regeneration oil product equipment in a kind of organic carbon, the oil smoke extraction regeneration oil product extracting method of the utility model is by changing mixing oil density and oil after liquefying, enable more than miscella bubbles through the water column, using oil pumping pumped, product oil is isolated with oil-water separator, product oil is finally imported into product tank, on-condensible gas includes at least methane, ethane gas ingredient, methane, the fuel gas such as ethane are eventually for burning, the heat of burning is used to supply miscellaneous equipment, the utility model device is suitable for processing carbide furnace high temperature flue gas, foul gas, the oil smoke of middle and high concentration, advantage is that investment is low, harmless treatment, this row is at low cost, floor space is small, it is easy to operate, destructor plant for environmental protection administration's approval is promoted the use of.The miscella that absorption tower bottom comes out can be used, and often subtract the production of catalytic cracking cyclic regeneration waste oil device.
Description
Technical field
The utility model is related to hydrocarbon treatment technologies, particularly relate to the oil smoke in a kind of organic carbon
Extraction regeneration oil product equipment.
Background technology
The main component of house refuse can be produced into for inorganic matter, old metal organic matter and moisture, inorganic matter slag etc.
Building material brick, old metal are extracted as metal, raw material to the organic substances such as organic matter waste plastics, scrap rubber anaerobic and negative oxygen carbonization
Stove high temperature is carbonized, and the high-temperature oil smoke gaseous solvents for producing coke coal and high concentration absorb Catalytic processes.In carbide furnace out
Flue gas, most of is hydrocarbon, and part acid and water are all presented in the form of steam state in flue gas, and in life, there are many carbon
Oxygen compound rubbish, traditional processing mode are usually burning disposal, and the pernicious gas for burning generation is evaporated into air, to ring
Cause very big influence in border.When burning away the refuse, organic matter is contained in rubbish, contains carbon in the tail gas generated when organic matter is burnt
The on-condensible gases such as oxygen compound, vapor, methane, these gases discharge in air and cause environmental pollution.
Utility model content
For deficiency of the prior art, the technical problem to be solved by the present invention is to provide a kind of organic matter carbon
Oil smoke extraction regeneration oil product equipment in change.
In order to solve the above technical problems, the utility model is realized by following scheme：Oil smoke in organic carbon carries
Regeneration oil product equipment is taken, which includes：
Absorption tower, the absorption tower include pedestal and the flue gas processing device being set on pedestal, the chassis interior setting
There is cavity volume, which connects with the cavity volume of the flue gas processing device, and the first water-cooled cooling of setting fills in the cavity volume of the pedestal
It puts, pedestal madial wall is provided with magnetic flap level gauge, and lateral wall bottom is provided with fuel-displaced interface tube, the fuel-displaced interface tube
The first oil well pump is provided on the pipeline of connection；Fixed gas discharge interface, inner cavity are provided at the top of the flue gas processing device
Be equipped with from top to bottom the second water-cooling cooling device, 2 set solid phase filler at regular intervals, be stacked in the solid phase filler
Ceramic ring, and mounting hole is provided on side wall of the height less than next solid phase filler, bend pipe is provided on the mounting hole, it is described
Bend pipe is opening up flue gas processing device inner cavity, external interface connection smoke inlet pipe, a upper solid phase filler and the
Several divergence expression nozzles are provided between two water-cooling cooling devices；
Miscella tank for storing miscella, is equipped with oil inlet interface, outer wall lower part is provided at the top of the miscella tank
Oil out port, product oil interface, which connects the divergence expression nozzle by oil pipe, and second is provided in pipeline
Oil well pump；
Solvent oil tank, for storage of solvent oil, the solvent roof is equipped with oil inlet interface, and outer wall lower part is provided with
Oil out port, which connects the divergence expression nozzle by oil pipe, and third oil well pump is provided in pipeline；
Condenser, the condenser be water circulation cooling device, top by oil pipe connect the miscella tank into
Oily interface, bottom connect the oil inlet interface of first oil well pump, solvent oil tank by oil pipe respectively；
Oil-water separator for the moisture in miscella and impurity oil to be separated, is left required product oil,
Oil inlet end connects the product oil interface of the miscella tank by pipeline, and top is provided with product oil interface, product oil interface
Product tank is connected by pipeline；
Double-pipe condenser, described sleeve pipe condenser connect the fixed gas discharge interface at the top of absorption tower, casing by pipeline
Condenser is built-in with water-cooling apparatus；
Gas tank, the gas tank are built-in with third water-cooling cooling device, top is provided with outlet for accommodating fixed gas
Interface；
Water seal, water is provided in the water seal, and tank body connects gas tank, and the tracheae being placed in the water seal by tracheae
Water surface is placed in hereinafter, being provided with outlet interface at the top of the water seal, side wall is connected with water inlet pipe and outlet pipe；
Burner, the burner connect the outlet interface of the water seal by tracheae.
Further, first water-cooling cooling device is coil pipe, and lower end connection water inlet pipe, upper end connects water outlet
Pipe crosses water in coil pipe, for miscella heat exchange, miscella is made to cool down.
Further, the lateral wall of the pedestal is provided with emptying interface, which is connected with evacuated tube, the emptying
Pipe is convenient to overhaul for miscella to be emptied；
The lateral wall of the pedestal is additionally provided with the first manhole, and first manhole is closed, is used for when not in use
Chassis interior is overhauled.
Further, the turning bottom of the bend pipe is provided with aperture.
Further, it is provided with spark arrester on the smoke inlet pipe.
Further, the lateral wall of the gas tank is provided with the second manhole.
Further, it is provided with valve on the oil pipe between the oil-water separator and miscella tank；
Valve is provided on the miscella tank oil inlet pipe；
Valve is provided in the top oil outlet pipe of the condenser；
Valve is provided in pipeline between the solvent oil tank and the condenser；
Pipeline, third oil well pump between second oil well pump and the divergence expression nozzle and the divergence expression nozzle it
Between pipeline be provided with valve；
Valve is provided in the outlet pipe of the gas tank；
Valve is provided in the outlet pipe of the water seal, the second back-fire relief is provided between the valve and the burner
Device, second check-valve, second check-valve connect burner by pipeline.
Relative to the prior art, the beneficial effects of the utility model are：The utility model discloses a kind of organic carbons
In oil smoke extraction regeneration oil product equipment, the utility model oil smoke extraction regeneration oil product extracting method be by change liquefy after
Mixing oil density and oil, enable more than miscella bubbles through the water column, using oil pumping pumped, to be detached with oil-water separator
Go out product oil, product oil is finally imported into product tank, on-condensible gas includes at least methane, ethane gas ingredient, methane, ethane
Waiting fuel gas, for the heat of burning for supplying miscellaneous equipment, the utility model device is suitable for processing carbon eventually for burning
Change the oil smoke of stove high temperature flue gas, foul gas, middle and high concentration, advantage is to invest low, harmless treatment, this row is at low cost, accounts for
Ground area is small, easy to operate, and the destructor plant for environmental protection administration's approval is promoted the use of.The miscella that absorption tower bottom comes out can
Using, often subtract catalytic cracking cyclic regeneration waste oil device production.
Description of the drawings
Fig. 1 is the oil smoke extraction regeneration oil product equipment connecting relation schematic diagram in the utility model organic carbon；
Fig. 2 is the utility model absorption tower structure diagram；
Fig. 3 is the utility model gas tank structure diagram.
Specific embodiment
The preferred embodiment of the utility model is described in detail below in conjunction with the accompanying drawings, so that the advantages of the utility model
It can be easier to be readily appreciated by one skilled in the art with feature, it is apparent clear and definite so as to be made to the scope of protection of the utility model
Define.
Please refer to attached drawing 1-3, the oil smoke extraction regeneration oil product equipment in a kind of organic carbon of the utility model, this sets
It is standby to include：
Absorption tower 5, which includes pedestal and the flue gas processing device being set on pedestal, the chassis interior are set
Cavity volume is equipped with, which connects with the cavity volume of the flue gas processing device, the first water-cooled cooling of setting in the cavity volume of the pedestal
Device 53, pedestal madial wall are provided with magnetic flap level gauge 54, and lateral wall bottom is provided with fuel-displaced interface tube 55, it is described go out
The first oil well pump 16 is provided on the pipeline that tubing interface 55 connects；Fixed gas row is provided at the top of the flue gas processing device
Outgoing interface, inner cavity are equipped with the second water-cooling cooling device 51,2 and set solid phase filler 52 at regular intervals, institute from top to bottom
It states and ceramic ring is stacked in solid phase filler, and mounting hole is provided on side wall of the height less than next solid phase filler 52, in the peace
Bend pipe 58 is provided on dress hole, the bend pipe 58 is in the opening up of flue gas processing device inner cavity, external interface connection flue gas
Air inlet pipe 12 is provided with several divergence expression nozzles 50 between upper 52 and second water-cooling cooling device 51 of a solid phase filler；
Ceramic ring built in solid phase filler 52, a large amount of ceramic ring is stacked in the container of solid phase filler, and when initial, solvent naphtha is from hair
Formula nozzle 50 is dissipated to spray, initial solvent naphtha is 100% single oil plant, when solvent oil tank 3 continues oil return, can by solvent naphtha and
Oil mixing in flue gas, then pumpback to solvent oil tank 3, after solvent naphtha is diluted to a certain degree, is generally diluted to solvent naphtha
When accounting is 20%, then the oil in flue gas can be cooled down and the oil in flue gas is made to form liquid by the solvent naphtha more renewed, solvent naphtha,
It mixes with solvent naphtha, is fallen downwards along ceramic ring after mixing, finally fallen in the cavity volume of bottom；
Miscella tank 2, for storing miscella, 2 top of miscella tank is equipped with oil inlet interface, the setting of outer wall lower part
There are oil out port, product oil interface, which connects the divergence expression nozzle 50 by oil pipe, and is provided in pipeline
Second oil well pump 14；
Solvent oil tank 3, for storage of solvent oil, 3 top of solvent oil tank is equipped with oil inlet interface, the setting of outer wall lower part
There is oil out port, which connects the divergence expression nozzle 50 by oil pipe, and third oil well pump is provided in pipeline
15；
Condenser 4, the condenser 4 are water circulation cooling device, and top connects the miscella tank 2 by oil pipe
Oil inlet interface, bottom connect the oil inlet interface of first oil well pump 16, solvent oil tank 3 by oil pipe respectively；
Oil-water separator 1 for the moisture in miscella and impurity oil to be separated, is left required product oil,
Its oil inlet end connects the product oil interface of the miscella tank 2 by pipeline, and top is provided with product oil interface, and product oil connects
Mouth passes through pipeline and connects product tank 13；
Double-pipe condenser 6, described sleeve pipe condenser 6 connect the fixed gas discharge interface at 5 top of absorption tower, set by pipeline
Pipework condensation device 6 is built-in with water-cooling apparatus；
Gas tank 7, the gas tank 7 are built-in with third water-cooling cooling device 71, top is provided with for accommodating fixed gas
Outlet interface；
Water seal 8 is provided with water in the water seal 8, and tank body connects gas tank 7 by tracheae, and is placed in the water seal 8
Tracheae to be placed in water surface hereinafter, 8 top of the water seal is provided with outlet interface, and side wall is connected with water inlet pipe and outlet pipe；
Burner 9, the burner 9 connect the outlet interface of the water seal 8 by tracheae.
First water-cooling cooling device 53 is coil pipe, and lower end connection water inlet pipe, upper end connects outlet pipe, coil pipe
It is interior cross water, for miscella heat exchange, miscella is made to cool down.
The lateral wall of the pedestal is provided with emptying interface 56, which is connected with evacuated tube, and the emptying is effective
It is emptied in by miscella, it is convenient to overhaul；
The lateral wall of the pedestal is additionally provided with the first manhole 57, and first manhole 57 is closed when not in use,
For being overhauled to chassis interior.
The turning bottom of the bend pipe 58 is provided with aperture 59.
Spark arrester 11 is provided on the smoke inlet pipe 12.
The lateral wall of the gas tank 7 is provided with the second manhole 72.
Valve is provided on oil pipe between the oil-water separator 1 and miscella tank 2；
Valve is provided on 2 oil inlet pipe of miscella tank；
Valve is provided in the top oil outlet pipe of the condenser 4；
Valve is provided in pipeline between the solvent oil tank 3 and the condenser 4；
Pipeline, third oil well pump 15 and the divergence expression between second oil well pump 14 and the divergence expression nozzle 50
Pipeline between nozzle 50 is provided with valve；
Valve is provided in the outlet pipe of the gas tank 7；
Valve is provided in the outlet pipe of the water seal 8, the second back-fire relief is provided between the valve and the burner 9
Device 17, second check-valve 18, second check-valve 18 connect burner 9 by pipeline.
The regeneration oil product extracting method of the equipment of the utility model, the extracting method include the following steps：
Step 1, flue gas contain hydrocarbon, and hydrocarbon is at least containing oil, vapor, fixed gas ingredient, high temperature
Flue gas enters pipeline (flue-gas temperature of the smoke inlet on absorption tower is below 500 degrees Celsius) through smoke inlet pipe 12, and passes through
Spark arrester 11 imports absorption tower 5 from bend pipe 58, and high-temperature flue gas moves upwards, through 2 solid phase fillers 52；
Solid phase filler 52 is by solvent naphtha and filler by smoke filtration, and the oil and solvent naphtha for making oil smoke mix, with fixed gas
Body detaches, and on-condensible gas continues up；
Step 2 opens the valve on third suction pump oil pipe, starts third oil well pump (15), and third oil well pump (15) will
Solvent naphtha is evacuated to divergence expression nozzle 50, and divergence expression nozzle 50 sprays solvent naphtha, and solvent naphtha is made to be come into full contact with the flue gas risen,
Ceramic ring built in solid phase filler 52, a large amount of ceramic ring is stacked in the container for filling up solid phase filler, and when initial, solvent naphtha is from divergence expression
Nozzle 50 sprays, and initial solvent naphtha is 100% single oil plant, can be by solvent naphtha and flue gas when solvent oil tank 3 continues oil return
In oil mixing, then pumpback to solvent oil tank 3, after solvent naphtha is diluted to a certain degree, then the solvent naphtha more renewed, solvent
Oil in flue gas can be cooled down and the oil in flue gas is made to form liquid by oil, mixed with solvent naphtha, fallen downwards along ceramic ring after mixing,
Finally fall in the cavity volume of bottom；Vapor liquefies through 2 solid phase fillers 52 and flows into pedestal cavity volume, and on-condensible gas is through the second water cooling
Heat sink 51 cools down；
Step 3, on-condensible gas further cools down through double-pipe condenser 6, and imports gas tank 7 by tracheae, in gas tank 7
Third water-cooling cooling device 71 again cools down to on-condensible gas, and the on-condensible gas after cooling imports water seal 8, fixed gas by tracheae
Body is imported in the water body inside water seal 8, is prevented on-condensible gas back draft, is finally exported on-condensible gas to burning by tracheae
Device 9, the heat that burner 9 is sent out are used to heating or being used to prepare other products for needing to heat to miscellaneous equipment；
Step 4, the oil water mixture processing in pedestal：
Since the oil density in flue gas is 0.95-0.98cm3, oil water mixture makes solvent naphtha molten with oil phase using densimetry
Change density, with production product solvent naphtha and the molten change density of oil phase, the density of miscella is made to be converted into 0.85-0.9g/cm3,
The mixing top that oil swims on water；
Step 5, the miscella in step 4 are evacuated to condenser 4 by the first oil well pump 16, make the reduction of miscella oil temperature,
Miscella imports miscella tank 2 from 4 top of condenser by oil pipe, and part miscella imports solvent oil tank 3, and solvent oil tank 3 is held
It is continuous that divergence expression nozzle 50 is imported by third oil well pump 15, it recycles；
Step 6, miscella tank 2 store miscella, and part miscella imports divergence expression nozzle by the second oil well pump 14
50, it recycles；
Step 7, the part miscella of miscella tank 2 are transported to oil-water separator 1, and oil-water separator 1 is by miscella
Moisture and impurity separation, the product oil after separation import finished pot 13 by oil pipe.
All of above cooling device connects cooling tower by water pipe, reaches water circulation use.
In above step, the flue-gas temperature that smoke inlet pipe 12 enters is 180-350 DEG C, and the temperature in ceramic ring is 50-
100 DEG C, the oil temperature of 5 bottom cavity volume of absorption tower is 50 DEG C hereinafter, the temperature in gas tank 7 is 50 DEG C hereinafter, each water-cooling apparatus
It is room temperature into water water temperature.
The extraction regeneration oil product operation principle of the utility model oil smoke extraction regeneration oil product equipment is as follows：
Hydrocarbon is collected as oil product tailing oil, separation oil, moisture, on-condensible gas, and on-condensible gas purification is burning
Gas accomplishes three kinds of substance separation of oil-water-gas.
Intermiscibility and insoluble, the volume change relationship of densimetry and oil-water-gas vapour phase liquid phase using Oil, Water, Gas, really
Determine processing unit.
Oil density after flue gas newly liquefaction is larger in 0.95-0.98g/cm3Although oily, similar density incompatible with water,
Therefore the oil after liquefying coexists with water, formation W/O, oil in water, it is therefore necessary to change the density of oil, with production product solvent
Oil makes the density of oil be converted into 0.85-0.9g/cm with the molten density that changes of oil phase3。
The oil product feedstock oil isolated is in case refining production, the solvent naphtha produced do oil recovery use again.
The fixed gases such as the methane in tail gas are insoluble with oil product, mutually put down with gas phases such as methane in filler from tower top spray oil product
Weighing apparatus, is mutually dissolved contact, oil product is absorbed in tail gas, tail gas separation, purification, for doing combustion gas.
In absorption tower set solid packing, and with inside and outside reflow method by the organic solvent that nozzle sprays in solid phase filler
On, it is come into full contact with flue gas, and carry out comprehensive heat exchange balance, the steam state made in flue gas that gas-liquid exchanges, gas-liquid mixes
Hydrocarbon becomes liquid from gaseous state and mixes with spraying into the solvent of condensation, becomes miscella and flows into tower, and the water of rising steams warp
Bottom of towe is fallen into as liquid after double phegmas, the foul gas of rising includes sour vapour and toxic gas in Ta Nei and phegma
Catalyst haptoreaction be decomposed and be dissolved in the vapor in flue gas and condensed water and fall into bottom of towe.
Light molecule is not also condensed into liquid by the condenser of tower top, does not coagulate referred to as insoluble in the solvent in tower in flue gas
Gas if methane ethane etc. enters by gas-guide tube in fixed gas tank, using gas burner burns, is heated to common brick or is separately done
It is used.
Safety in production, the high-temperature flue gas that carbide furnace comes out can burn or explode in air, therefore before flue gas enters tower
Spark arrester is added, fixed gas tempering can set off an explosion, and can cause equipment detonation, and before burner plus water seal dress, isolation burning things which may cause a fire disaster hinder
Only burn.
This equipment is suitable for the oil smoke of processing carbide furnace high temperature flue gas, foul gas, middle and high concentration, and advantage is investment
Low, harmless treatment, this row is at low cost, and floor space is small, easy to operate, and the destructor plant for environmental protection administration's approval is promoted
It uses.The miscella that absorption tower bottom comes out can be used, and often subtract the production of catalytic cracking cyclic regeneration waste oil device.
Above description is merely a prefered embodiment of the utility model, not thereby limits the patent model of the utility model
Enclose, every equivalent structure or equivalent flow shift made based on the specification and figures of the utility model directly or
It connects and is used in other relevant technical fields, be equally included in the patent within the scope of the utility model.
Claims (7)
1. the oil smoke extraction regeneration oil product equipment in organic carbon, which is characterized in that the equipment includes：
Absorption tower (5), the absorption tower (5) include pedestal and the flue gas processing device being set on pedestal, and the chassis interior is set
Cavity volume is equipped with, which connects with the cavity volume of the flue gas processing device, the first water-cooled cooling of setting in the cavity volume of the pedestal
Device (53), pedestal madial wall are provided with magnetic flap level gauge (54), and lateral wall bottom is provided with fuel-displaced interface tube (55),
The first oil well pump (16) is provided on the pipeline of fuel-displaced interface tube (55) connection；It is provided at the top of the flue gas processing device
Fixed gas discharge interface, inner cavity be equipped with from top to bottom the second water-cooling cooling device (51), 2 set solid phase at regular intervals
Filler (52) is stacked with ceramic ring in the solid phase filler, and is provided on side wall of the height less than next solid phase filler (52)
Mounting hole, is provided with bend pipe (58) on the mounting hole, the bend pipe (58) in the opening up of flue gas processing device inner cavity,
External interface connection smoke inlet pipe (12), is provided between a upper solid phase filler (52) and the second water-cooling cooling device (51)
Several divergence expression nozzles (50)；
Miscella tank (2) for storing miscella, is equipped with oil inlet interface, the setting of outer wall lower part at the top of the miscella tank (2)
There are oil out port, product oil interface, which connects the divergence expression nozzle (50) by oil pipe, and is set in pipeline
There is the second oil well pump (14)；
Solvent oil tank (3) for storage of solvent oil, is equipped with oil inlet interface, the setting of outer wall lower part at the top of the solvent oil tank (3)
There is oil out port, which connects the divergence expression nozzle (50) by oil pipe, and third oil pumping is provided in pipeline
It pumps (15)；
Condenser (4), the condenser (4) are water circulation cooling device, and top connects the miscella tank (2) by oil pipe
Oil inlet interface, bottom connected respectively by oil pipe first oil well pump (16), solvent oil tank (3) oil inlet interface；
Oil-water separator (1) for the moisture in miscella and impurity oil to be separated, is left required product oil,
Oil inlet end connects the product oil interface of the miscella tank (2) by pipeline, and top is provided with product oil interface, and product oil connects
Mouth passes through pipeline and connects product tank (13)；
Double-pipe condenser (6), described sleeve pipe condenser (6) connect the fixed gas discharge interface at the top of absorption tower (5) by pipeline,
Double-pipe condenser (6) is built-in with water-cooling apparatus；
Gas tank (7), the gas tank (7) are built-in with third water-cooling cooling device (71), top is set for accommodating fixed gas
There is outlet interface；
Water seal (8), the water seal (8) is interior to be provided with water, and tank body connects gas tank (7) by tracheae, and is placed in the water seal (8)
Interior tracheae will be placed in water surface hereinafter, being provided with outlet interface at the top of the water seal (8), and side wall is connected with water inlet pipe and goes out
Water pipe；
Burner (9), the burner (9) connect the outlet interface of the water seal (8) by tracheae.
2. the oil smoke extraction regeneration oil product equipment in organic carbon according to claim 1, it is characterised in that：Described
One water-cooling cooling device (53) is coil pipe, and lower end connection water inlet pipe, upper end connection outlet pipe, coil pipe is interior to cross water, is used for
With miscella heat exchange, miscella is made to cool down.
3. the oil smoke extraction regeneration oil product equipment in organic carbon according to claim 1, it is characterised in that：The bottom
The lateral wall of seat is provided with emptying interface (56), which is connected with evacuated tube, which is used for miscella
Emptying, it is convenient to overhaul；
The lateral wall of the pedestal is additionally provided with the first manhole (57), and first manhole (57) is closed when not in use,
For being overhauled to chassis interior.
4. the oil smoke extraction regeneration oil product equipment in organic carbon according to claim 1, it is characterised in that：It is described curved
The turning bottom of pipe (58) is provided with aperture (59).
5. the oil smoke extraction regeneration oil product equipment in organic carbon according to claim 1, it is characterised in that：The cigarette
Spark arrester (11) is provided in gas air inlet pipe (12).
6. the oil smoke extraction regeneration oil product equipment in organic carbon according to claim 1, it is characterised in that：The gas
The lateral wall of tank (7) is provided with the second manhole (72).
7. the oil smoke extraction regeneration oil product equipment in organic carbon according to claim 1, it is characterised in that：
Valve is provided on oil pipe between the oil-water separator (1) and miscella tank (2)；
Valve is provided on miscella tank (2) oil inlet pipe；
Valve is provided in the top oil outlet pipe of the condenser (4)；
Valve is provided in pipeline between the solvent oil tank (3) and the condenser (4)；
Pipeline, third oil well pump (15) and the diverging between second oil well pump (14) and the divergence expression nozzle (50)
Pipeline between formula nozzle (50) is provided with valve；
Valve is provided in the outlet pipe of the gas tank (7)；
Valve is provided in the outlet pipe of the water seal (8), the second back-fire relief is provided between the valve and the burner (9)
Device (17), second check-valve (18), second check-valve (18) connect burner (9) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721355316.8U CN207596787U (en) | 2017-10-19 | 2017-10-19 | Oil smoke extraction regeneration oil product equipment in organic carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721355316.8U CN207596787U (en) | 2017-10-19 | 2017-10-19 | Oil smoke extraction regeneration oil product equipment in organic carbon |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207596787U true CN207596787U (en) | 2018-07-10 |
Family
ID=62755687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721355316.8U Expired - Fee Related CN207596787U (en) | 2017-10-19 | 2017-10-19 | Oil smoke extraction regeneration oil product equipment in organic carbon |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207596787U (en) |
-
2017
- 2017-10-19 CN CN201721355316.8U patent/CN207596787U/en not_active Expired - Fee Related
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