CN109289446A - A kind of petroleum refining desulphurization system - Google Patents

A kind of petroleum refining desulphurization system Download PDF

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Publication number
CN109289446A
CN109289446A CN201811312313.5A CN201811312313A CN109289446A CN 109289446 A CN109289446 A CN 109289446A CN 201811312313 A CN201811312313 A CN 201811312313A CN 109289446 A CN109289446 A CN 109289446A
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CN
China
Prior art keywords
desulfurization
pipe
outlet pipe
flue
chamber
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CN201811312313.5A
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Chinese (zh)
Inventor
彭圆
杨大鹏
吴国良
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Individual
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Priority to CN201811312313.5A priority Critical patent/CN109289446A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
    • B01D53/1468Removing hydrogen sulfide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
    • B01D53/1481Removing sulfur dioxide or sulfur trioxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor

Abstract

The invention belongs to desulphurization plant technical fields, specifically a kind of petroleum refining desulphurization system, enter pipe, desulfurization outlet pipe, desulfurization chamber and agitating unit including flue, desulfurization, flue is set to above the ground by bracket, desulfurization chamber is arranged in ground, desulfurization chamber is located at the lower section of flue, desulfurization indoor storage absorbing liquid;Desulfurization enters pipe and desulfurization outlet pipe bilateral symmetry is obliquely installed, desulfurization enters pipe and desulfurization outlet pipe between flue and desulfurization chamber, desulfurization enters pipe and desulfurization outlet pipe upper end is communicated with flue respectively, desulfurization enter pipe and desulfurization outlet pipe lower end respectively with communicated inside desulfurization chamber, desulfurization, which enters, is arranged reserve tank on pipe and desulfurization outlet pipe side wall, reserve tank due to be used to make the centrifugal force in flue gas when spiral plate rotation the metallic particles that throws away enter reserve tank and realize and collect, desulfurization, which enters, is arranged bypass damper in the flue between pipe and desulfurization outlet pipe.The present invention improves desulfurization effect.

Description

A kind of petroleum refining desulphurization system
Technical field
The invention belongs to desulphurization plant technical field, specifically a kind of petroleum refining desulphurization system.
Background technique
Petroleum is the more complicated system of composition component, it is mainly mixed by different hydrocarbons, It comprises many elements such as sulphur, oxygen, nitrogen, phosphorus, during petroleum refining, need to take a variety of physics or chemistry side Petroleum is become the different cultivars such as gasoline, diesel oil, liquefied petroleum gas by method.Under existing situation, people are increasingly heavier to environmental protection Depending on, and gasoline is in combustion, it will usually sulfur dioxide gas is generated, this gas will cause huge pollution to environment; So during petroleum refining, it will usually which the element sulphur in petroleum is carried out deeper desulfurization process, the mesh done so Be in order to which the sulfur content extracted in gasoline is able to maintain within the scope of defined.In desulfurizer, it is based on stone Lime stone-gypsum wet method occupies mainstream, wherein also mostly using spray pattern.The atomizing desulfurizer is in absorption tower Absorbing liquid containing wet type desulfurizing agent is sprayed to smoke evacuation, to carry out using absorbing liquid to the oxysulfide in smoke evacuation in absorption tower Desulfurization, existing desulfurizer have that desulfurization effect is undesirable.
Summary of the invention
In order to make up for the deficiencies of the prior art, a kind of petroleum refining desulphurization system proposed by the present invention.The present invention mainly uses How desulfuration efficiency is improved during solving the problems, such as petroleum refining.
The technical solution adopted by the present invention to solve the technical problems is: a kind of petroleum refining desulfurization system of the present invention System, including flue, desulfurization enter pipe, desulfurization outlet pipe, desulfurization chamber and agitating unit, and the flue is set on ground by bracket Desulfurization chamber is arranged in side, ground, and desulfurization chamber is located at the lower section of flue, desulfurization indoor storage absorbing liquid;The desulfurization enters pipe and desulfurization Outlet pipe bilateral symmetry is obliquely installed, and desulfurization enters pipe and desulfurization outlet pipe between flue and desulfurization chamber, and desulfurization enters pipe and desulfurization goes out Pipe upper end is communicated with flue respectively, desulfurization enter pipe and desulfurization outlet pipe lower end respectively with communicated inside desulfurization chamber, desulfurization enters pipe and de- Reserve tank is set on sulphur outlet pipe side wall, the metal that reserve tank is thrown away due to be used to make the centrifugal force in flue gas when spiral plate rotation Grain enters reserve tank and realizes collection, and desulfurization, which enters, is arranged bypass damper in the flue between pipe and desulfurization outlet pipe, desulfurization enters Guan Yu The spray head tilted down is arranged in the connection position of flue, and setting pump and water pipe, water pipe upper end and desulfurization enter in pipe in desulfurization chamber Spray head is connected, and the indoor absorbing liquid of desulfurization is sprayed into desulfurization by spray head and enters pipe by pump, enters flue gas after pipe just in entrance desulfurization Start to be absorbed by liquid absorption;
The agitating unit include shaft, driving unit, No.1 gear, agitating paddle, spiral plate, lifting magnet, magnet block and No.1 bevel gear, the shaft are vertically installed in desulfurization chamber, and No.1 gear is installed in shaft lower part, and shaft passes through above desulfurization chamber Driving unit realize rotation;The agitating paddle is mounted on the lower end of shaft, agitating paddle be used for the indoor absorbing liquid of desulfurization into Coming into full contact with for row stirring, realization absorbing liquid and flue gas, improves desulfurization effect;The desulfurization enters to be respectively provided in pipe and desulfurization outlet pipe Spiral plate, and the spiral plate that desulfurization enters in pipe and desulfurization outlet pipe is oppositely oriented, spiral plate uses segmentation structure, and spiral plate connects The end of touching connects firmly lifting magnet respectively, and adjacent magnets disk is mutually exclusive, lifting magnet periphery setting magnet block, on adjacent magnets disk Magnet block attracts each other, and the No.1 bevel gear engaged with No.1 gear is installed in the spiral plate end of bottom respectively;The spiral The idler wheel that plate is arranged by surface is contacted with the tube wall that desulfurization enters pipe and desulfurization outlet pipe.When work, bypass damper closing is made into cigarette Gas enters desulfurization and enters pipe, and driving unit drives shaft rotation, makes spiral by the engaged transmission of No.1 gear and No.1 bevel gear Plate rotation, desulfurization, which enters, to be separated from each other between the adjoining spiral plate in pipe due to the presence of lifting magnet, while the presence of magnet block So that the spiral plate of lower section is driven the spiral plate rotation of top, is not only rotated while also in generation so that desulfurization enters the spiral plate in pipe Lower movement makes desulfurization enter the flue gas in pipe and adequately mixes, and the indoor absorbing liquid of desulfurization is sprayed into desulfurization by spray head and enters pipe by pump, Flue gas is set just to start to be absorbed by liquid absorption after entering pipe into desulfurization, after flue gas enters desulfurization chamber, the cigarette under the drive of agitating paddle Gas further comes into full contact with absorbing liquid, makes desulfurization effect more preferably, and the flue gas after desulfurization enters desulfurization outlet pipe in the band of spiral plate Dynamic lower discharge, comes back in flue, spiral plate is contacted by idler wheel with the tube wall that desulfurization enters pipe and desulfurization outlet pipe, on the one hand right Spiral plate plays the effect of support, on the other hand reduces the frictional force between spiral plate and tube wall, improves service life.
Thickness gradually increases the spiral plate from top to bottom;The idler wheel is mounted on spiral plate by support plate;It is described Slot is set in support plate, support plate blocks spiral plate by slot and realizes installation, and the slot of the support plate on spiral plate from On gradually increase down.Idler wheel is mounted on spiral plate by the card slot being arranged in support plate, has the thickness of spiral plate gradually to become Change, in spiral plate rotation, the card slot and spiral plate of support plate can be realized close contact, ensure that the stabilization of support plate.
Limited block is arranged in the end face that the No.1 bevel gear connect with spiral plate;The upper end of the limited block and No.1 gear Face forms face contact, to limit moving down for No.1 bevel gear.Since No.1 bevel gear is in heeling condition, in gravity Under, spiral plate and No.1 bevel gear be easy to happen downslide, and the extruding between upper surface that limited block passes through No.1 gear hinders The only downslide of No.1 bevel gear ensure that No.1 bevel gear engages with the normal of No.1 gear, improve the stability of work.
Groove is arranged in the end face of the limited block and No.1 Gear Contact, and elastic balloon is arranged in groove;The desulfurization chamber Aeration head is arranged in bottom, and aeration head is connected by tracheae and check valve with elastic balloon.Limited block turns with No.1 bevel gear When dynamic, due to the relative rotation between limited block and No.1 gear, elastic balloon is made to generate compression, the compression that elastic balloon generates Air is sprayed by aeration head, is accelerated the movement of absorbing liquid and the disturbance of flue gas, is further improved absorbing liquid to flue gas Desulfurization effect.
The driving unit includes fixed cylinder, sleeve, fixed case, wind wheel and bevel gear set, and the fixed cylinder is mounted on de- The top of sulphur room, fixed cylinder top connect firmly sleeve, and sleeve passes through flue upper end and installs fixed case;The shaft upper end, which passes through, to be fixed Cylinder and sleeve simultaneously extend to inside fixed case;The wind wheel is rotatably installed on fixed case, and wind wheel passes through setting in fixed case The rotation of bevel gear set drive shaft;Perforative venthole, venthole and fixed case are provided with inside the shaft in the axial direction It communicates, the air hole that extraneous air is introduced to fixed case is set on wind wheel, is blown into the air of wind wheel through air hole and venthole Into desulfurization chamber, the mixed effect of flue gas and absorbing liquid in desulfurization chamber is improved.Wind wheel passes through bevel gear set under the drive of wind-force Shaft rotation is driven, reduces the consumption of fossil energy, reduces costs.
The U-typed gas flow that setting is communicated with desulfurization chamber in the fixed cylinder;The desulfurization outlet pipe is connected with desulfurization chamber Logical one end is arranged baffle, and baffle goes out for making the indoor gas of desulfurization only pass through U-typed gas flow just and can enter desulfurization It manages, the spiral plate of bottom passes through baffle by rotation axis and connect with No.1 bevel gear in desulfurization outlet pipe;The shaft is located at solid Flabellum is arranged in part in safety barrel, and thermal vias is arranged on fixed cylinder side wall.The design of U-typed gas flow and block makes desulfurization Indoor flue gas need to could be discharged through U-typed gas flow, and the time for retaining the indoor flue gas of desulfurization in desulfurization chamber is longer, Absorbing liquid is extended to effective desulfurization time of flue gas, desulfurization effect is more preferable, and flabellum is rotated with shaft, accelerates in fixed cylinder The convection current of outer air plays the effect of cooling to the flue gas in the U-typed gas flow of fixed cylinder.
Beneficial effects of the present invention are as follows:
1. a kind of petroleum refining desulphurization system of the present invention, the present invention is by desulfurization entering that segmented is arranged in pipe Spiral plate makes to be in state of disturbance, after flue gas enters desulfurization chamber, the flue gas under the drive of agitating paddle into the indoor flue gas of desulfurization It is come into full contact with absorbing liquid, makes desulfurization effect more preferably.
2. a kind of petroleum refining desulphurization system of the present invention, the present invention is set by setting block and in fixed cylinder U-typed gas flow is set, extends absorbing liquid to effective desulfurization time of flue gas, desulfurization effect is more preferable.
Detailed description of the invention
Fig. 1 is main view of the invention;
Fig. 2 is A-A cross-sectional view in Fig. 1 of the present invention;
Fig. 3 is partial enlarged view at B in Fig. 1 of the present invention;
Fig. 4 is partial enlarged view at C in Fig. 1 of the present invention;
Fig. 5 is the schematic diagram that idler wheel of the present invention is mounted on spiral plate by support plate;
In figure: flue 1, desulfurization enter pipe 2, desulfurization outlet pipe 3, desulfurization chamber 4, agitating unit 5, bracket 11, reserve tank 21, bypass Valve 12, shaft 51, driving unit 52, No.1 gear 53, agitating paddle 54, spiral plate 55, lifting magnet 56, magnet block 57, No.1 Bevel gear 58, support plate 7, slot 71, limited block 8, elastic balloon 10, aeration head 9, fixed cylinder 521, sleeve 522, is consolidated idler wheel 6 Determine case 523, wind wheel 524, bevel gear set 525, U-typed gas flow 526, baffle 31, flabellum 59.
Specific embodiment
It is carried out using a kind of petroleum refining desulphurization system of Fig. 1-Fig. 5 to an embodiment of the present invention as described below.
As shown in figures 1 and 3, a kind of petroleum refining desulphurization system of the present invention, including flue 1, desulfurization enter pipe 2, Desulfurization outlet pipe 3, desulfurization chamber 4 and agitating unit 5, the flue 1 are set to above the ground by bracket 11, and desulfurization chamber is arranged in ground 4, desulfurization chamber 4 is located at the lower section of flue 1, stores absorbing liquid in desulfurization chamber 4;The desulfurization enters 3 bilateral symmetry of pipe 2 and desulfurization outlet pipe It is obliquely installed, desulfurization enters pipe 2 and desulfurization outlet pipe 3 between flue 1 and desulfurization chamber 4, and desulfurization enters 3 upper end of pipe 2 and desulfurization outlet pipe It is communicated respectively with flue 1, desulfurization enters pipe 2 and 3 lower end of desulfurization outlet pipe is communicated with inside desulfurization chamber 4 respectively, and desulfurization enters pipe 2 and desulfurization Reserve tank 21 is set on 3 side wall of outlet pipe, and reserve tank 21 is used to make in flue gas the centrifugal force when spiral plate 55 rotates due to throws away Metallic particles enters reserve tank 21 and realizes collection, and desulfurization, which enters, is arranged bypass damper 12 in the flue 1 between pipe 2 and desulfurization outlet pipe 3, Desulfurization enters pipe 2 and the spray head tilted down is being arranged with the connection position of flue 1, setting pump and water pipe, water pipe upper end in desulfurization chamber 4 Enter the spray head in pipe 2 with desulfurization to be connected, the absorbing liquid in desulfurization chamber 4 is sprayed into desulfurization by spray head and enters pipe 2 by pump, and flue gas is made to exist Just start to be absorbed by liquid absorption after entering pipe 2 into desulfurization;
The agitating unit 5 includes shaft 51, driving unit 52, No.1 gear 53, agitating paddle 54, spiral plate 55, magnet Disk 56, magnet block 57 and No.1 bevel gear 58, the shaft 51 are vertically installed in desulfurization chamber 4, and No.1 is installed in 51 lower part of shaft Gear 53, shaft 51 realize rotation by the driving unit 52 of 4 top of desulfurization chamber;The agitating paddle 54 is mounted under shaft 51 End, agitating paddle 54 are realized coming into full contact with for absorbing liquid and flue gas, are improved de- for being stirred to the absorbing liquid in desulfurization chamber 4 Sulphur effect;The desulfurization, which enters, is respectively provided with spiral plate 55 in pipe 2 and desulfurization outlet pipe 3, and desulfurization enters the spiral shell in pipe 2 and desulfurization outlet pipe 3 Rotating plate 55 is oppositely oriented, and spiral plate 55 uses segmentation structure, and the end that spiral plate 55 is in contact connects firmly lifting magnet 56, phase respectively Adjacent lifting magnet 56 is mutually exclusive, and magnet block 57 is arranged in 56 periphery of lifting magnet, and the magnet block 57 on adjacent magnets disk 56 attracts each other, 55 end of spiral plate of bottom is installed by the No.1 bevel gear 58 engaged with No.1 gear 53 respectively;The spiral plate 55 passes through table The idler wheel 6 of face setting is contacted with the tube wall that desulfurization enters pipe 2 and desulfurization outlet pipe 3.When work, by bypass damper 12 closing make flue gas into Enter desulfurization and enter pipe 2, driving unit 52 drives shaft 51 to rotate, and is made by No.1 gear 53 and the engaged transmission of No.1 bevel gear 58 Spiral plate 55 rotates, and desulfurization, which enters, to be separated from each other between the adjoining spiral plate 55 in pipe 2 due to the presence of lifting magnet 56, while magnetic The spiral plate 55 that the presence of iron block 57 makes the spiral plate 55 of lower section drive top rotates, so that desulfurization enters the spiral plate 55 in pipe 2 Not only rotation also moves up and down simultaneously, and the flue gas for entering desulfurization in pipe 2 adequately mixes, and pumps the absorption in desulfurization chamber 4 Liquid sprays into desulfurization by spray head and enters pipe 2, makes flue gas just start to be absorbed by liquid absorption after entering pipe 2 into desulfurization, flue gas enters de- Behind sulphur room 4, flue gas is further come into full contact with absorbing liquid under the drive of agitating paddle 54, makes desulfurization effect more preferably, after desulfurization Flue gas enters desulfurization outlet pipe 3 and is discharged under the drive of spiral plate 55, comes back in flue 1, and spiral plate 55 is by idler wheel 6 and takes off Sulphur enters the tube wall contact of pipe 2 and desulfurization outlet pipe 3, and the effect of support is on the one hand played to spiral plate 55, on the other hand makes spiral Frictional force between plate 55 and tube wall reduces, and improves service life.
As shown in figure 5, thickness gradually increases the spiral plate 55 from top to bottom;The idler wheel 6 is mounted on by support plate 7 On spiral plate 55;Slot 71 is set in the support plate 7, and support plate 7 blocks spiral plate 55 by slot 71 and realizes installation, and spiral shell The slot 71 of support plate 7 on rotating plate 55 gradually increases from top to bottom.Idler wheel 6 is mounted on by the card slot being arranged in support plate 7 On spiral plate 55, the thickness of spiral plate 55 is gradually changed, and when spiral plate 55 rotates, the card slot and spiral plate 55 of support plate 7 can It realizes and is in close contact, and because the size of slot 71 is also constantly to increase from top to bottom, so that idler wheel 6 is evenly distributed on spiral plate On 55, the stabilization of support plate 7 ensure that.
As shown in Figure 1 and Figure 4, limited block 8 is arranged in the end face that the No.1 bevel gear 58 connect with spiral plate 55;The limit The upper surface of position block 8 and No.1 gear 53 forms face contact, to limit moving down for No.1 bevel gear 58.Due to No.1 bevel gear 58 are in heeling condition, and under the effect of gravity, spiral plate 55 and No.1 bevel gear 58 are easy to happen downslide, limited block 8 by with The downslide squeezed to prevent No.1 bevel gear 58 between the upper surface of No.1 gear 53, ensure that No.1 bevel gear 58 and No.1 The normal engagement of gear 53, improves the stability of work.
As shown in figure 4, the end face setting groove that the limited block 8 is contacted with No.1 gear 53, groove is interior to be arranged elastic gas Capsule 10;Aeration head 9 is arranged in 4 bottom of desulfurization chamber, and aeration head 9 is connected by tracheae and check valve with elastic balloon 10.Limit When position block 8 is rotated with No.1 bevel gear 58, due to the relative rotation between limited block 8 and No.1 gear 53, make elastic balloon 10 generate compression, and the compressed air that elastic balloon 10 generates is sprayed by aeration head 9, accelerate raising and being atomized for absorbing liquid, And then the contact area of absorbing liquid and flue gas is increased, absorbing liquid is further improved to the desulfurization effect of flue gas.
As shown in Figure 1, the driving unit 52 includes fixed cylinder 521, sleeve 522, fixed case 523, wind wheel 524 and cone tooth Wheel group 525, the fixed cylinder 521 are mounted on the top of desulfurization chamber 4, and sleeve 522 is connected firmly above fixed cylinder 521, and sleeve 522 passes through 1 upper end of flue is installed by fixed case 523;51 upper end of shaft passes through fixed cylinder 521 and sleeve 522 and extends to fixed case 523 It is internal;The wind wheel 524 is rotatably installed on fixed case 523, the bevel gear set 525 that wind wheel 524 passes through setting in fixed case 523 Drive shaft 51 rotates;Perforative venthole, venthole and 523 phase of fixed case are provided with inside the shaft 51 in the axial direction It is logical, the air hole that extraneous air is introduced to fixed case 523 is set on wind wheel 524, be blown into the air of wind wheel 524 through air hole and Venthole enters desulfurization chamber 4, improves the mixed effect of flue gas and absorbing liquid in desulfurization chamber 4, while can play the effect of cooling. Wind wheel 524 drives shaft 51 to rotate under the drive of wind-force by bevel gear set 525, reduces the consumption of fossil energy, reduces Cost.
As depicted in figs. 1 and 2, the U-typed gas flow 526 that setting is communicated with desulfurization chamber 4 in the fixed cylinder 521;Institute One end setting baffle 31 that desulfurization outlet pipe 3 is connected with desulfurization chamber 4 is stated, baffle 31 is used to make the gas in desulfurization chamber 4 only to pass through Crossing U-typed gas flow 526 just can enter desulfurization outlet pipe 3, and the spiral plate 55 of bottom is passed through by rotation axis in desulfurization outlet pipe 3 Baffle 31 is connect with No.1 bevel gear 58;The shaft 51 is located at the setting of the part in fixed cylinder 521 flabellum 59, fixed cylinder 521 Thermal vias is set on side wall.The design of U-typed gas flow 526 and block makes the flue gas in desulfurization chamber 4 need to be through U-typed gas Runner 526 could be discharged, and the time for retaining the flue gas in desulfurization chamber 4 in desulfurization chamber 4 is longer, extend absorbing liquid to flue gas Effective desulfurization time, desulfurization effect is more preferable, flabellum 59 with shaft 51 rotate, accelerate pair of 521 inner air and outer air of fixed cylinder Stream, the effect of cooling is played to the flue gas in the U-typed gas flow 526 of fixed cylinder 521.
Detailed process is as follows:
When work, so that flue gas is entered desulfurization the closing of bypass damper 12 and enter pipe 2, driving unit 52 drives shaft 51 to rotate, Rotate spiral plate 55 by the engaged transmission of No.1 gear 53 and No.1 bevel gear 58, desulfurization enters the adjoining spiral plate in pipe 2 It is separated from each other between 55 due to the presence of lifting magnet 56, while the presence of magnet block 57 makes the spiral plate 55 of lower section drive top Spiral plate 55 rotate, not only rotate while also moving up and down so that desulfurization enters the spiral plate 55 in pipe 2, desulfurization is made to enter pipe Flue gas in 2 adequately mixes, and the absorbing liquid in desulfurization chamber 4 is sprayed into desulfurization by spray head and enters pipe 2 by pump, keeps flue gas de- in entrance Sulphur just starts to be absorbed by liquid absorption after entering pipe 2, after flue gas enters desulfurization chamber 4, under the drive of agitating paddle 54 flue gas further with Absorbing liquid comes into full contact with, and makes desulfurization effect more preferably, and the flue gas after desulfurization enters desulfurization outlet pipe 3 and arranges under the drive of spiral plate 55 Out, it comes back in flue 1, spiral plate 55 is contacted by idler wheel 6 with the tube wall that desulfurization enters pipe 2 and desulfurization outlet pipe 3, on the one hand right Spiral plate 55 plays the effect of support, on the other hand reduces the frictional force between spiral plate 55 and tube wall, improves use Service life.
Idler wheel 6 is mounted on spiral plate 55 by the card slot being arranged in support plate 7, has the thickness of spiral plate 55 gradually to become Change, when spiral plate 55 rotates, the card slot and spiral plate 55 of support plate 7 can be realized close contact, ensure that the steady of support plate 7 It is fixed.
Since No.1 bevel gear 58 is in heeling condition, under the effect of gravity, spiral plate 55 and No.1 bevel gear 58 are easy It glides, the downslide squeezed to prevent No.1 bevel gear 58 between the upper surface that limited block 8 passes through No.1 gear 53 is protected It has demonstrate,proved No.1 bevel gear 58 to engage with the normal of No.1 gear 53, has improved the stability of work.
When limited block 8 is rotated with No.1 bevel gear 58, due to the relative rotation between limited block 8 and No.1 gear 53, Elastic balloon 10 is set to generate compression, the compressed air that elastic balloon 10 generates is sprayed by aeration head 9, accelerates the fortune of absorbing liquid Dynamic and flue gas disturbance, further improves absorbing liquid to the desulfurization effect of flue gas.
Wind wheel 524 drives shaft 51 to rotate under the drive of wind-force by bevel gear set 525, reduces disappearing for fossil energy Consumption, reduces costs.
The design of U-typed gas flow 526 and block makes the flue gas in desulfurization chamber 4 need to be through 526 ability of U-typed gas flow Discharge, the time for retaining the flue gas in desulfurization chamber 4 in desulfurization chamber 4 is longer, extends effective desulfurization of the absorbing liquid to flue gas Time, desulfurization effect is more preferable, and flabellum 59 is rotated with shaft 51, the convection current of 521 inner air and outer air of fixed cylinder is accelerated, to fixed cylinder Flue gas in 521 U-typed gas flow 526 plays the effect of cooling.
More than, it is illustrated about one embodiment of the present invention, but the present invention is not limited to the above embodiments, It does not depart from and is able to carry out various changes in the range of present subject matter.
Industrial applicibility
According to the present invention, by entering to be arranged in pipe the spiral plate of segmented in desulfurization, make to enter at the indoor flue gas of desulfurization In state of disturbance, after flue gas enters desulfurization chamber, flue gas comes into full contact with absorbing liquid under the drive of agitating paddle, makes desulfurization effect more It is good, so that this petroleum refining desulphurization system is useful in desulphurization plant field.

Claims (6)

1. a kind of petroleum refining desulphurization system, it is characterised in that: enter pipe (2) including flue (1), desulfurization, desulfurization outlet pipe (3), take off Sulphur room (4) and agitating unit (5), the flue (1) are set to above the ground by bracket (11), and desulfurization chamber (4) are arranged in ground, Desulfurization chamber (4) is located at the lower section of flue (1), stores absorbing liquid in desulfurization chamber (4);The desulfurization enters pipe (2) and desulfurization outlet pipe (3) Bilateral symmetry is obliquely installed, and desulfurization enters pipe (2) and desulfurization outlet pipe (3) is located between flue (1) and desulfurization chamber (4), and desulfurization enters pipe (2) communicated respectively with flue (1) with desulfurization outlet pipe (3) upper end, desulfurization enter pipe (2) and desulfurization outlet pipe (3) lower end respectively with desulfurization It is communicated inside room (4), desulfurization enters setting reserve tank (21), desulfurization on pipe (2) and desulfurization outlet pipe (3) side wall and enters pipe (2) and desulfurization Bypass damper (12) are set in flue (1) between outlet pipe (3), desulfurization enter pipe (2) the connection position with flue (1) be arranged to Under inclined spray head, setting pump and water pipe, water pipe upper end enter the spray head in pipe (2) with desulfurization and are connected in desulfurization chamber (4);
The agitating unit (5) includes shaft (51), driving unit (52), No.1 gear (53), agitating paddle (54), spiral plate (55), lifting magnet (56), magnet block (57) and No.1 bevel gear (58), the shaft (51) are vertically installed in desulfurization chamber (4), No.1 gear (53) are installed in shaft (51) lower part, and shaft (51) realizes rotation by the driving unit (52) above desulfurization chamber (4); The agitating paddle (54) is mounted on the lower end of shaft (51), and agitating paddle (54) is for stirring the absorbing liquid in desulfurization chamber (4) It mixes, realizes coming into full contact with for absorbing liquid and flue gas, improve desulfurization effect;The desulfurization enters to be all provided in pipe (2) and desulfurization outlet pipe (3) It sets spiral plate (55), and desulfurization oppositely oriented, spiral plate (55) end that enters the spiral plate (55) in pipe (2) and desulfurization outlet pipe (3) The No.1 bevel gear (58) engaged with No.1 gear (53) is installed respectively;The idler wheel that the spiral plate (55) is arranged by surface (6) tube wall for entering pipe (2) and desulfurization outlet pipe (3) with desulfurization contacts.
2. a kind of petroleum refining desulphurization system according to claim 1, it is characterised in that: the spiral plate (55), which uses, divides Segmentation structure, the end that spiral plate (55) is in contact connect firmly lifting magnet (56) respectively, and adjacent magnets disk (56) is mutually exclusive, magnet Magnet block (57) are arranged in disk (56) periphery, and the magnet block (57) on adjacent magnets disk (56) attracts each other.
3. a kind of petroleum refining desulphurization system according to claim 1, it is characterised in that: the No.1 bevel gear (58) with Limited block (8) are arranged in the end face of spiral plate (55) connection;The limited block (8) and the upper surface forming face of No.1 gear (53) connect Touching, to limit moving down for No.1 bevel gear (58).
4. a kind of petroleum refining desulphurization system according to claim 3, it is characterised in that: the limited block (8) and No.1 Groove is arranged in the end face of gear (53) contact, and elastic balloon (10) are arranged in groove;Aeration head is arranged in desulfurization chamber (4) bottom (9), aeration head (9) is connected by tracheae and check valve with elastic balloon (10).
5. a kind of petroleum refining desulphurization system according to claim 1, it is characterised in that: the driving unit (52) includes Fixed cylinder (521), sleeve (522), fixed case (523), wind wheel (524) and bevel gear set (525), fixed cylinder (521) peace It mounted in the top of desulfurization chamber (4), is connected firmly sleeve (522) above fixed cylinder (521), sleeve (522) is installed across flue (1) upper end Fixed case (523);Shaft (51) upper end passes through fixed cylinder (521) and sleeve (522) and extends in fixed case (523) Portion;The wind wheel (524) is rotatably installed on fixed case (523), the cone tooth that wind wheel (524) passes through setting in fixed case (523) Wheel group (525) drive shaft (51) rotation;It is provided with perforative venthole, venthole in the axial direction inside the shaft (51) It is communicated with fixed case (523), the air hole that extraneous air is introduced to fixed case (523) is set on wind wheel (524).
6. a kind of petroleum refining desulphurization system according to claim 5, it is characterised in that: set in the fixed cylinder (521) Set the U-typed gas flow (526) communicated with desulfurization chamber (4);One end that the desulfurization outlet pipe (3) is connected with desulfurization chamber (4) It is arranged baffle (31), baffle (31) could be into for making the gas in desulfurization chamber (4) only pass through U-typed gas flow (526) Enter desulfurization outlet pipe (3), the spiral plate (55) of desulfurization outlet pipe (3) interior bottom passes through baffle (31) by rotation axis and No.1 bores tooth Take turns (58) connection.
CN201811312313.5A 2018-11-06 2018-11-06 A kind of petroleum refining desulphurization system Withdrawn CN109289446A (en)

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CN201085985Y (en) * 2007-09-10 2008-07-16 中电投远达环保工程有限公司 Double-return circuit spray column
CN101229478A (en) * 2007-01-22 2008-07-30 宝山钢铁股份有限公司 Gas outburst spinning dive desulfurization dust cleaning apparatus
KR20130095470A (en) * 2012-02-20 2013-08-28 이달은 Chiyong chapter pyrolysis gas / oil in the exhaust gas guiding device that contains
CN104815528A (en) * 2015-04-14 2015-08-05 上海交通大学 Wet smoke self-temperature returning integrated smoke purification device and application thereof
CN105263603A (en) * 2013-06-06 2016-01-20 株式会社Ihi Desulfurization device
CN105688634A (en) * 2016-02-26 2016-06-22 刘佩佩 Desulfuration device based on spiral gas-liquid mixing and rotational flow gas-liquid separating principle
CN108159847A (en) * 2018-01-11 2018-06-15 重庆交通大学 A kind of energy-saving environmental-protection flue gas purification plant based on injection mixing

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101229478A (en) * 2007-01-22 2008-07-30 宝山钢铁股份有限公司 Gas outburst spinning dive desulfurization dust cleaning apparatus
CN201085985Y (en) * 2007-09-10 2008-07-16 中电投远达环保工程有限公司 Double-return circuit spray column
KR20130095470A (en) * 2012-02-20 2013-08-28 이달은 Chiyong chapter pyrolysis gas / oil in the exhaust gas guiding device that contains
CN105263603A (en) * 2013-06-06 2016-01-20 株式会社Ihi Desulfurization device
CN104815528A (en) * 2015-04-14 2015-08-05 上海交通大学 Wet smoke self-temperature returning integrated smoke purification device and application thereof
CN105688634A (en) * 2016-02-26 2016-06-22 刘佩佩 Desulfuration device based on spiral gas-liquid mixing and rotational flow gas-liquid separating principle
CN108159847A (en) * 2018-01-11 2018-06-15 重庆交通大学 A kind of energy-saving environmental-protection flue gas purification plant based on injection mixing

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Application publication date: 20190201