CN108261899A - For the equipment of offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge - Google Patents
For the equipment of offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge Download PDFInfo
- Publication number
- CN108261899A CN108261899A CN201711464557.0A CN201711464557A CN108261899A CN 108261899 A CN108261899 A CN 108261899A CN 201711464557 A CN201711464557 A CN 201711464557A CN 108261899 A CN108261899 A CN 108261899A
- Authority
- CN
- China
- Prior art keywords
- ceramic
- cabinet
- equipment
- recharge
- carbon dioxide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/22—Separation 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 diffusion
- B01D53/228—Separation 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 diffusion characterised by specific membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D17/00—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces
- F25D17/02—Arrangements for circulating cooling fluids; Arrangements for circulating gas, e.g. air, within refrigerated spaces for circulating liquids, e.g. brine
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Abstract
The invention discloses a kind of equipment for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge, including the net desulfurization device of ceramic module, cleaner, liquid circulation cabinet, waste liquid cabinet, sulfate cabinet, fluid infusion cabinet, cool down equipment, supercharging equipment, online detection instrument and automatic control system, the boiler waste gas removes dust particles therein by cleaner, oil droplet etc., subsequently into the net desulfurization device of ceramic module, it sulfur dioxide in flue gas and is chemically reacted in the alkaline solution of ceramic-film tube internal circulation flow, exhaust gas after desulfurization carries out the backfill of submarine oil exploitation by supercharger.This method is economic and environment-friendly, and desulfuration efficiency is high, and device volume is small, saves using space, especially suitable for job platforms such as offshore production platforms.
Description
Technical field
The invention belongs to environmentally friendly exhaust-gas treatment field more particularly to dioxy caused by offshore production platform operation carrier
Change sulphur exhaust gas and carry out purified treatment.
Background technology
Marine fuel and offshore production platform boiler oil after combustion, can be generated containing oxysulfide (hereinafter
SOX), nitrogen oxides (hereinafter NOX) etc. substances, these substances can be discharged into air in the form of exhaust gas.And SOXIn
SO2, acid rain can be formed in an atmosphere, and harm is generated to environment and the mankind.It administers sulfur dioxide and has become global common recognition, it is international
International Maritime Organization (IMO) (IMO)《《73/78 anti-pollution convention》(MARPOL pacts) supplemental provisions VI requirements：I.e. from 2012, in high sea row
The sulphur content of fuel oil of the foreign-going ship made has to be lower than 3.5% (m/m), and 0.5% (m/m) is would fall to the year two thousand twenty, and this
Scheme completes feasibility and examines and will be carried out earlier than 2018.
Offshore production platform boiler oil is using the crude oil just exploited, and many sulfur materials are contained in the inside, at present state
Interior all offshore production platforms are all without applying any desulphurization plant, currently without a set of technology maturation and suitable for offshore oil production
The desulfurization program and product of platform, how to handle the sulfur dioxide of its generation is current problem to be solved.
Existing flue gas desulfunzation device is sprayed into lye in the form of spraying in exhaust gas using wet desulphurization is sprayed, with
Exhaust gas mixes, through chemically reacting SO in exhaust gasX、NOXIt captures and enters in liquid phase, achieve the purpose that purification.But exhaust gas is generally high
Temperature, lye spray into meeting partial gasification in exhaust gas, are discharged together with exhaust gas, it is possible to cause secondary pollution.And spray process can generate
A large amount of waste water containing a large amount of flue dust, oil, heavy metal etc. in waste water, needs to increase complicated waste water treatment system, increases energy
Consumption increases cost, and bulky spray tower systems are not advantageously mounted on production platform.
In currently used equipment, there are one liquid in-out mouths, and liquid is not completely filled in many ceramic-film tubes or is not had
There is liquid, cause desulfuration efficiency low and the waste to ceramic-film tube.Secondly it is influenced, is filled by temperature in practical applications
Deformation can be generated by putting, and lead to ceramic tube fracture or ceramic tube and outer loop pipeline Joint failure.Or in transportational process
Jolting or shaking leads to failure of apparatus.In addition, ceramic membrane is impermeable layer used by the device, membrane aperture size is on a 10nm left sides
The right side, in sweetening process, the easy fouling of ceramic vessel wall blocks ceramic membrane nano-pore, and desulfuration efficiency is caused to reduce and is even lost completely
Effect.
Invention content
For overcome the deficiencies in the prior art, the purpose of the present invention is to provide for offshore production platform exhuast gas desulfurization and
The equipment of carbon dioxide recovery recharge and application.
In order to achieve the above objectives, the present invention is achieved by the following technical solutions.
A kind of equipment for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge, including the net gas of ceramic module
Desulfurizer, cleaner, liquid circulation cabinet, cooling equipment, supercharging equipment；
Boiler flue gas outlet by flue successively with the cleaner, the gas of the net desulfurization device of ceramic module
Body channel, supercharging equipment series connection；
The fluid passage of the net desulfurization device of the liquid circulation cabinet, ceramic module, cooling equipment by alkali lye pipeline according to
Secondary series connection forming circuit, alkali lye pipeline are equipped with lye delivery pump, flowmeter, pressure sensor, temperature sensor and lye valve
Door.
Further the net desulfurization device of the ceramic module include ceramic-film tube, at least two porous plates, at least four
Cooling shaft, goes out liquid water row, U-tube at feed liquor water row；
Preceding porous plate and rear porous plate are attached fixed support by four cooling shafts, form cube box, Duo Getao
Porcelain membrane tube, which is inserted into the hole in preceding porous plate and rear porous plate, forms ceramic-film tube array, neighbouring two ceramic membrane pipe ends
Portion is connected and sealed with U-tube, and each column ceramic-film tube is made to connect, and each column ceramic-film tube bottom opening direction it is consistent,
The top opening direction is consistent, and the top opening connection feed liquor water row of ceramic-film tube array, bottom opening connects out liquid water
Row.Contain the hole of quantity identical with ceramic-film tube number of rows in water row, to ensure that often row's ceramic-film tube is filled with liquid.It makes full use of
Every ceramic-film tube, improves desulfuration efficiency.
Further the ceramic-film tube uses water permeable membrane, 50~500nm of membrane aperture.Membrane aperture is larger to be conducive in exhaust gas
SOXAlkaline reaction is entered by ceramic-film tube, can also reduce, slow down the ceramic membrane nano-pore caused by ceramic membrane tube wall incrustation
When blocking, while being cleaned with water pressurization, scale forming matter can discharge ceramic-film tube with water, and then realize the clear of ceramic membrane
The purpose of ceramic Pore Blocking is washed and avoided, prevents the failure of ceramic membrane.
Capsule is further equipped between the ceramic-film tube end and U-tube, Capsule is two elastic colloid cylinders
It composes in parallel, the small-bore of Capsule is sleeved on the end of two ceramic-film tubes, and U-tube inner wall sleeve is two ceramic-film tube ends, outside
Wall is inserted into the inside of Capsule, and glue is filled in the gap between three.The design of U-tube and Capsule can realize ceramic tube two
Two elastic connections, the stress that monoblock connection is avoided to generate, so as to improve the service life of ceramic-film tube, and can substantially reduce
Bond glue dosage, be tightly connected together compared to entire ceramic-film tube end can reduce by 75% glue quantity.
Further the cooling shaft is one way sleeve structure, and import and export is formed by cooling pipe and cooling equipment
Circuit.The deformation that high-temp waste gas brings cooling shaft is reduced, so as to ensure that porous Board position is relatively fixed, is reduced to extending there through
Ceramic-film tube stress.
Further the alkali lye pipeline is equipped with Venturi tube, the outlet of liquid circulation cabinet and the inlet of Venturi tube
Connection, the liquid outlet first branch pipeline of Venturi tube are connect with cooling equipment importation, the liquid sucting port and ceramic die of Venturi tube
The liquid channel outlet connection of the net desulfurization device of block, liquid outlet the second branch pipeline and the net qi exhaustion of ceramic module of Venturi tube
The fluid passage import connection of sulphur device.So that the operation of ceramic membrane liquid in pipe is recycled by the form of negative pressure, to protect
Card liquid is not permeated by ceramic-film tube.
Waste liquid cabinet, cleaning cabinet are further further included, cleaning cabinet is exported leads to the liquid of the net desulfurization device of ceramic module
Road import is connected by Cleaning pipes, and Cleaning pipes are equipped with pump, and waste liquid cabinet is located at below the net desulfurization device of ceramic module, gives up
The import of liquid cabinet is connect with the exhaust gases passes import of the net desulfurization device of ceramic module by waste solution channel.
Fluid infusion cabinet, sulfate cabinet are further further included, fluid infusion cabinet is connect by liquid supplementation channel with liquid circulation cabinet, liquid
Circulating tank is connect by sulfate pipeline with sulfate cabinet.
Threeway is further equipped on the flue between the net desulfurization device of the ceramic module and supercharging equipment
Valve.The exhaust gas volumn into supercharging equipment is reconciled by reconciling triple valve 1003.
The application of exhuast gas desulfurization and carbon dioxide recovery recharge equipment at sea in production platform is further additionally provided,
Offshore production platform boiler waste gas removes solid phase therein, liquid phase impurity by cleaner, subsequently into the net gas of ceramic module
Desulfurizer removes sulfur dioxide in flue gas, and the exhaust gas after desulfurization is backfilled by supercharging equipment into submarine oil goaf；
Lye in liquid circulation cabinet enters the inlet of Venturi tube by lye delivery pump, then flow through venturi
Liquid outlet first branch pipeline is returning liquid circulation cabinet by cooling down equipment, goes out the imbibition of liquid water row's connection Venturi tube
Mouthful, the liquid outlet the second branch pipeline of feed liquor water row's connection Venturi tube, so as to which lye be allowed to be recycled in ceramic tube, with cigarette
Sulfur dioxide chemically reacts in gas, when alkaline reaction enters sulfate when completely or nearly the reaction was complete in liquid circulation cabinet
Cabinet decrease temperature crystalline is separated by filtration to obtain sulfate, then supplement fresh lye by fluid infusion cabinet and enter liquid circulation cabinet；
When the net desulfurization unit efficiency of ceramic module declines, ceramic-film tube is injected into the clean water pressurization in cleaning cabinet,
It recoils to ceramic-film tube, the waste water penetrated flows into waste liquid cabinet；
Recirculated cooling water is passed through in cooling shaft, reduces the deformation that high-temp waste gas brings cooling shaft.
Advantageous effect：Compared with prior art, the advantage of the invention is that：
1) U-tube and the structure design of water row can make desulfuration efficiency improve 7%；
2) design of U-tube and Capsule can save 75% glue, reduce production cost；
3) ceramic membrane technology is not directly contacted with by the exhaust gas in flue with absorbent, at the same again can selectivity absorption we
Required harmful substance and particulate matter；
4) exhaust gas after desulfurization can be used for the backfill after submarine oil exploitation, first, avoiding increasing carbon dioxide manufacture
Equipment reduces cost；Two can realize that waste gas recovery utilizes economic and environment-friendly purpose；
5) it can realize ceramic membrane cleaning function, extend the service life of ceramic membrane；
6) design of cooling shaft and U-tube and Capsule can reduce stress and the deformation during product use, improve
The quality of product and and stability.
Description of the drawings
Fig. 1 is a kind of sulfur removal technology figure for offshore production platform；
Fig. 2 is a kind of desulfurizer structure diagram for offshore production platform；
Fig. 3 is a kind of cooling shaft structure chart of desulfurizer for offshore production platform；
Fig. 4 is that a kind of water of desulfurizer for offshore production platform arranges structure chart；
Fig. 5 is a kind of Capsule structure chart of desulfurizer for offshore production platform；
Fig. 6 is a kind of automatic control system figure for offshore production platform；
In figure, the net desulfurization device of 1. ceramic modules, the net gas modular unit of 100. ceramics, 101. lye delivery pumps, 102.
First lye valve, 103. first wash-out valves, 104. second lye valves, 105. temperature sensors, 106. Venturi tubes,
107. the second wash-out valve, 108. third lye valves, 109. first pressure sensors, 1090. second pressure sensors,
1001. smoke inlets, 1002. exhanst gas outlets, 1003. flue gas triple valves, 1004. flue gas flow meters,
11. go out liquid water row, 110. flowmeters, 111. lye export flanges, 122. lye import flanges,
12. feed liquor water is arranged,
13. axis is removed cold, 131. outlet(discharge) flanges, 132. suction flanges,
14. ceramic-film tube,
Porous plate after 16., porous plate in 17., porous plate before 18.,
19. Capsule, 193. small-bores,
2. liquid circulation cabinet, 200. sewage draining valves,
3. fluid infusion cabinet, 301. fluid infusion pump,
4. sulfate cabinet, 401. sulfuric acid salt pumps,
5. equipment is cooled down, 501. cooling pumps,
6. cleaner, 7. boilers, 8. supercharging equipments, 10. cleaning cabinets, 20. waste collection cabinets；
600. signal acquisitions and control unit, 601. interchangers, 602. display units, 603. main distribution boards, 604. sensings
Device, 605. keyboards, mouse, 606. printers.
Specific embodiment
Below in conjunction with present example and attached drawing, clear, complete description is carried out to the technical solution in the present invention, is shown
Right described embodiment is only part of the embodiment of the present invention.Based on the embodiments of the present invention, ordinary skill
Personnel do not make creation type labour under the premise of all other embodiments obtained all in the scope of protection of the invention.
As shown in Figure 1, a kind of equipment for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge, including pottery
The net desulfurization device 1 of ceramic former block, cleaner 6, liquid circulation cabinet 2, cooling equipment 5, supercharging equipment 8, on-line monitoring equipment and
Automatic control system；Boiler flue gas outlet is filled by flue with the cleaner 6, the net desulfurization of ceramic module successively
Put 1 gas passage, supercharging equipment 8 is connected；The fluid passage of the net desulfurization device 1 of liquid circulation cabinet 2, ceramic module, cooling
Equipment 5 is sequentially connected in series forming circuit by alkali lye pipeline, and alkali lye pipeline is equipped with lye delivery pump 101, flowmeter 110, and first
Pressure sensor 109, second pressure sensor 1090, temperature sensor 105, the first lye valve 102, the second lye valve
104, third lye valve 108, each sensor and valve are connect respectively with signal acquisition and control unit 600.As shown in fig. 6, letter
Number acquisition and control unit 600 connect respectively cool down equipment 5, boiler 7, supercharging equipment 8, main distribution board 603, all kinds of valves, sensing
Device 604, interchanger 601 realize outputting and inputting for data-signal.Interchanger 601 connects display unit 602, printer respectively
606, keyboard, mouse 605 realize the real-time display of data and good man-machine interaction interface function.Main distribution board mainly connects
Connect all kinds of pumps such as lye delivery pump 101, fluid infusion pump 301, sulfuric acid salt pump 401, cooling pump 501.Signal acquisition and control unit 600
The input signal of each sensor is received, lye delivery pump 301, lye valve, cooling are controlled by PLC automatic control system
The operating of system stability and high efficiency is realized in the movement of pump 501 and each pipe valve.
In specific implementation, when 109 numerical value of first pressure sensor is less than setting value, setting value for -0.20 ±
0.01Mpa, signal collecting and controlling unit 600 receive the input signal from first pressure sensor 109, then output letter
Number, it turns the first lye valve 102, the second lye valve 104 down, reduces 10% every time, until reaching sets requirement；When the first pressure
When 109 numerical value of force snesor is more than setting value, setting value is -0.20 ± 0.01Mpa, and signal collecting and controlling unit 600 receives
To the input signal from first pressure sensor 109, then output signal, tunes up the first lye valve 102, the second lye valve
Door 104, increases by 10% every time, until reaching sets requirement.
When 110 numerical value of flowmeter is less than setting value, setting value is 70 ± 3LPM, and signal collecting and controlling unit 600 connects
The input signal for carrying out flowmeter 110 is received, then output signal, tune up the first lye valve 102, the second lye valve 104, often
It is secondary to increase by 10%, until reaching sets requirement；When 110 numerical value of flowmeter be more than setting value when, setting value be 70 ± 3LPM, signal
Acquisition and control unit 600 receive the input signal for carrying out flowmeter 110, and then output signal, turns the first lye valve down
102nd, the second lye valve 104, reduces 10% every time, until reaching sets requirement.
When the test number of temperature sensor 105 is less than setting value, setting value is 30 ± 3 DEG C, signal collecting and controlling
Unit 600 receives the input signal from temperature sensor 105, then output signal, turns the operation work(of plate cooling system 5 down
Rate reduces by 10% every time, until reaching setting value；When the test number of temperature sensor 105 is more than setting value, setting value is
30 ± 3 DEG C, signal collecting and controlling unit 600 receives the input signal from temperature sensor 105, then output signal,
The operation power of cooling system 5 is tuned up, increases by 10% every time, until reaching setting value.
When the test value of flue gas flow meter 1004 is more than setting value, signal collecting and controlling unit 600, which receives, to be come from
The input signal of flue gas flow meter 1004, allows rear input signal, turns flue gas triple valve 1003 down, reduces 5% every time, until reaching
Setting value；When the test value of flue gas flow meter 1004 is less than setting value, signal collecting and controlling unit 600 is received from cigarette
The input signal of air-flow gauge 1004, allows rear input signal, tunes up flue gas triple valve 1003, increases by 5% every time, is set until reaching
Definite value.
In specific example, temperature sensor can also be replaced with thermometer, pressure gauge replaces pressure sensor, Ge Gefa
Door can adjust realization manually using manually-operated gate, all operations；Or instrument and sensor are installed simultaneously, manually-operated gate and electricity
Movable valve can manually and automatically switch at any time.
The exhaust gas generated in boiler 7 reaches cleaner 6 by flue, removes solid phase therein, liquid phase impurity, such as
Dust particles, oil droplet etc., the smoke content in exhaust gas can drop to 5-30mg/m3, exhaust gas is arrived by pipeline after dedusting
Up to the net gas release unit 1 of ceramic module.
The net desulfurization device 1 of ceramic module includes main shell and the net gas modular unit 100 of internal ceramics, sees Fig. 2, ceramics
The net desulfurization device of module can include the net gas modular unit 100 of one or more ceramics, and the exhaust gas after dedusting enters cigarette
Gas entrance 1001, then exhaust gas rising is by the lye institute reactive absorption in ceramic net gas modular unit 100, giving up after desulfurization
Gas is discharged from exhanst gas outlet 1002.
Supercharging equipment 8 is reached from the exhaust gas that exhanst gas outlet 1002 is discharged through piping, a cigarette is installed before supercharging equipment 8
Gas triple valve 1003 and flue gas flow meter 1004.The flue gas into supercharging equipment can be reconciled by reconciling triple valve 1003
Amount.Flue gas can be squeezed into seabed goaf by supercharging equipment and be backfilled.
As shown in Fig. 2, the net desulfurization device of ceramic module include ceramic-film tube 14, it is preceding in after three blocks of porous plates, four it is cold
But axis 13, feed liquor water arrange 12, go out liquid water row 11, U-tube；Preceding porous plate 18, middle porous plate 17 and rear porous plate 16 are by four phases
Same is attached fixed support for connecting the stainless steel cooling shaft 13 of fixed porous plate, and multiple ceramic-film tubes 14 are more before being inserted into
Ceramic-film tube array is formed in hole in orifice plate 18, middle porous plate 17 and rear porous plate 16.Glue is used respectively in 14 both ends of ceramic-film tube
Cap 19 and U-tube are connected and sealed, and each column ceramic-film tube is allowed to be together in series respectively.19 small-bore 193 of Capsule is sleeved on ceramic membrane
The end of pipe, U-tube inner wall sleeve are inserted into the inside of Capsule 19 in ceramic-film tube end, outer wall 154.Capsule 19, ceramic-film tube 14
It is connected and sealed with U-tube three with high temperature glue, each column ceramic-film tube is made to connect, and each column ceramic-film tube bottom is opened
Mouth direction is consistent, the top opening direction is consistent, and the top opening connection feed liquor water row 12 of ceramic-film tube array, bottom is opened
Mouth connects out liquid water row 11, and feed liquor water row 12 is sealed with liquid water row 11 is gone out by lye export flange 111 and exterior line
Connection, so as to form circulation line.
The first wash-out valve 103 and the second wash-out valve 107 are closed, opens the first lye valve 102, the second lye valve
104 and third lye valve 108.Lye in circulating tank 2 enters the inlet of Venturi tube 106 by lye delivery pump 101,
Then the liquid outlet first branch pipeline of flow through venturi 106 is returning circulating tank 2 by cooling down equipment 5.Go out liquid water row 11
Connect the liquid sucting port of Venturi tube 106, the liquid outlet the second branch pipeline of 12 connection Venturi tube 106 of feed liquor water row, so as to allow
Lye is recycled in ceramic tube.In circulation line equipped with first pressure sensor 109 and second pressure sensor 1090,
Temperature sensor 105, flowmeter 110, monitor the lye of the cycle in pipeline on-line.It can be with when a certain numerical value change
Carry out the automatic movement for reconciling lye delivery pump, lye valve.
Fluid infusion cabinet 3 is squeezed into fresh lye in circulating tank 2 by fluid infusion pump 301.Such as when the conductivity value in circulating tank 2
During less than 115ms/cm, fluid infusion pump 301 can be opened, a certain amount of fresh lye is added in into circulating tank.
The cold suction flange 132 for removing axis 13 and the connection cooling equipment 5 of outlet(discharge) flange 131, opening cooling pump 501 allow in pipeline
Water recycled and axis 13 gone to cool down to cold.
The condenser pipe group being made of in trapezoidal enclosure more stainless steel tubes at smoke inlet 1001, the upper and lower of condenser pipe group connect
Mouth connects the export pipeline and inlet ductwork of cooling equipment 5 respectively, and flue gas is run from bottom to top, the realization pair of cooling water upper entering and lower leaving
The cooling of flue gas.Meanwhile more stainless steel condenser pipes can also realize the equally distributed effect to flue gas, improve desulfurization effect
Rate.
Opening sulfuric acid salt pump 401 can squeeze into liquid in circulating tank 2 in sulfate cabinet 4.Liquid drops in sulfate cabinet
Temperature is separated by filtration to obtain sulphate crystal, and clear liquid, which can recycle, to be reconfigured lye and recycled.
Containing a certain amount of seawater in cleaning cabinet 10, for the cleaning to ceramic-film tube.It is cleaned to ceramic-film tube
When, the first lye valve 102 and third lye valve 108 are first shut off, opens the first wash-out valve 103 and the second lye valve
104th, the second wash-out valve 107, adjusting the second wash-out valve 107 and the second lye valve 104 makes second pressure sensor 1090
Middle pressure reaches 0.1MPa or so, is positive pressure in ceramic-film tube, and seawater is easily washable ceramic fenestra, beats under the effect of the pressure
Sewage draining valve 200 is opened, the sewage penetrated flows into waste collection cabinet 20.
Embodiment 1
Boiler smoke tolerance is 12500Nm3, using fenestra 50-500nm aluminium oxide ceramics membrane tubes, internal diameter 10mm, wall thickness is
1.5mm, outer diameter 13mm, length 1m.The net desulfurization device of ceramic module contains there are two net gas modular unit, and total volume is
2.8m3.Lye uses 14% sodium hydroxide solution.Adjust the first lye valve 102, the second lye valve 104, third lye
Valve 108 is so that flow is 60L/min, and the temperature in control piper is at 30 DEG C or so in each net gas modular unit pipeline.
Actually measured cigarette data are shown in Table 1.Carbon dioxide does not absorb substantially as can be seen from Table 1, and the removal efficiency of sulfur dioxide is
97.1%.
1 embodiment of table, 1 test result table
| CO2%) | SO2ppm) | |
| Gas inlet 1001 | 6.26 | 350 |
| Exhanst gas outlet 1002 | 6.20 | 10 |
Embodiment 2
Boiler smoke tolerance is 12500Nm3, using fenestra 50-500nm aluminium oxide ceramics membrane tubes, internal diameter 10mm, wall thickness is
1.5mm, outer diameter 13mm, length 1m.The net desulfurization device of ceramic module contains there are two net gas modular unit, and total volume is
2.8m3.Lye uses 25% sodium hydroxide solution.Adjust the first lye valve 102, the second lye valve 104, third lye
Valve 108 is so that flow is 60L/min, and the temperature in control piper is at 30 DEG C or so in each net gas modular unit pipeline.
Actually measured cigarette data are shown in Table 2.Carbon dioxide does not absorb substantially as can be seen from Table 2, and the removal efficiency of sulfur dioxide is 88%.
2 embodiment of table, 2 test result table
| CO2%) | SO2ppm) | |
| Gas inlet 1001 | 6.27 | 350 |
| Exhanst gas outlet 1002 | 6.25 | 42 |
Embodiment 3
Boiler smoke tolerance is 12500Nm3, using fenestra 50-500nm aluminium oxide ceramics membrane tubes, internal diameter 10mm, wall thickness is
1.5mm, outer diameter 13mm, length 1m.The net desulfurization device of ceramic module contains there are two net gas modular unit, and total volume is
2.8m3.Lye is used by 25% sodium hydroxide solution and 15% sodium hydroxide solution by volume 1:1 carries out mixing group
Into.The first lye valve 102, the second lye valve 104, third lye valve 108 are adjusted so that each net gas module list
Flow is 70L/min in first pipeline, and the temperature in control piper is at 30 DEG C or so.Actually measured cigarette data are shown in Table 3.From table 3
It can be seen that carbon dioxide does not absorb substantially, the removal efficiency of sulfur dioxide is 96.6%.
3 embodiment of table, 3 test result table
| CO2%) | SO2ppm) | |
| Gas inlet 1001 | 6.28 | 350 |
| Exhanst gas outlet 1002 | 6.24 | 12 |
The present invention is illustrated according to above-described embodiment, it should be understood that above-described embodiment does not limit this in any form
Invention, all technical solutions obtained using equivalent substitution or equivalent transformation mode are within the scope of the present invention.
Claims (10)
1. a kind of equipment for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge, which is characterized in that including pottery
The net desulfurization device of ceramic former block, cleaner, liquid circulation cabinet, cooling equipment, supercharging equipment；
Boiler flue gas outlet is led to by gas of the flue successively with the cleaner, the net desulfurization device of ceramic module
Road, supercharging equipment series connection；
The fluid passage of the net desulfurization device of the liquid circulation cabinet, ceramic module, cooling equipment are gone here and there successively by alkali lye pipeline
Connection forming circuit, alkali lye pipeline are equipped with lye delivery pump, flowmeter, pressure sensor, temperature sensor and lye valve.
2. the equipment according to claim 1 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
Be characterized in that, the net desulfurization device of ceramic module include ceramic-film tube, at least two porous plates, at least four cooling shafts,
Feed liquor water row goes out liquid water row, U-tube；
Preceding porous plate and rear porous plate are attached fixed support by four cooling shafts, form cube box, multiple ceramic membranes
Pipe, which is inserted into the hole in preceding porous plate and rear porous plate, forms ceramic-film tube array, and neighbouring two ceramic-film tube ends are used
U-tube is connected and sealed, and each column ceramic-film tube is made to connect, and each column ceramic-film tube bottom opening direction is consistent, most upper
Square opening direction is consistent, and the top opening connection feed liquor water row of ceramic-film tube array, bottom opening connects out liquid water row.
3. the equipment according to claim 2 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, the ceramic-film tube uses water permeable membrane, 50 ~ 500nm of membrane aperture.
4. the equipment according to claim 2 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, Capsule is equipped between the ceramic-film tube end and U-tube, and Capsule is two elastic colloid cylinder parallel connection groups
Into the small-bore of Capsule is sleeved on the end of two ceramic-film tubes, and U-tube inner wall sleeve is inserted into two ceramic-film tube ends, outer wall
The inside of Capsule is filled with glue in the gap between three.
5. the equipment according to claim 2 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, the cooling shaft is one way sleeve structure, and import and export is formed into a loop by cooling pipe and cooling equipment.
6. the equipment according to claim 1 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, the alkali lye pipeline is equipped with Venturi tube, and the outlet of liquid circulation cabinet and the inlet of Venturi tube connect, text
The liquid outlet first branch pipeline of venturi is connect with cooling equipment importation, liquid sucting port and the net qi exhaustion of ceramic module of Venturi tube
The liquid channel outlet connection of sulphur device, liquid outlet the second branch pipeline and the net desulfurization device of ceramic module of Venturi tube
Fluid passage import connects.
7. the equipment according to claim 1 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, further include waste liquid cabinet, cleaning cabinet, the fluid passage import that cleaning cabinet exports with the net desulfurization device of ceramic module is led to
Over cleaning pipeline connects, and Cleaning pipes are equipped with pump, and waste liquid cabinet is located at ceramic module net desulfurization device lower section, waste liquid cabinet into
Mouth is connect with the exhaust gases passes import of the net desulfurization device of ceramic module by waste solution channel.
8. the equipment according to claim 1 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, further include fluid infusion cabinet, sulfate cabinet, fluid infusion cabinet is connect by liquid supplementation channel with liquid circulation cabinet, liquid circulation cabinet
It is connect by sulfate pipeline with sulfate cabinet.
9. the equipment according to claim 1 for offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge,
It is characterized in that, triple valve is equipped on the flue between the net desulfurization device of the ceramic module and supercharging equipment.
10. exhuast gas desulfurization and carbon dioxide recovery recharge equipment described in any one of claim 1 ~ 9 at sea production platform
In application.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711464557.0A CN108261899A (en) | 2017-12-28 | 2017-12-28 | For the equipment of offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge |
| CN201811629572.0A CN109464888A (en) | 2017-12-28 | 2018-12-28 | A kind of technique and its system for generation multielement hot fluid in ocean platform |
| CN201811629658.3A CN109464889A (en) | 2017-12-28 | 2018-12-28 | A kind of technique and its system for ocean platform gas cleaning |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711464557.0A CN108261899A (en) | 2017-12-28 | 2017-12-28 | For the equipment of offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108261899A true CN108261899A (en) | 2018-07-10 |
Family
ID=62772704
Family Applications (3)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711464557.0A Pending CN108261899A (en) | 2017-12-28 | 2017-12-28 | For the equipment of offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge |
| CN201811629572.0A Pending CN109464888A (en) | 2017-12-28 | 2018-12-28 | A kind of technique and its system for generation multielement hot fluid in ocean platform |
| CN201811629658.3A Pending CN109464889A (en) | 2017-12-28 | 2018-12-28 | A kind of technique and its system for ocean platform gas cleaning |
Family Applications After (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811629572.0A Pending CN109464888A (en) | 2017-12-28 | 2018-12-28 | A kind of technique and its system for generation multielement hot fluid in ocean platform |
| CN201811629658.3A Pending CN109464889A (en) | 2017-12-28 | 2018-12-28 | A kind of technique and its system for ocean platform gas cleaning |
Country Status (1)
| Country | Link |
|---|---|
| CN (3) | CN108261899A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110026405A (en) * | 2019-04-04 | 2019-07-19 | 北京卫星制造厂有限公司 | A kind of waste gas and waste liquid reclaimer based on recoverable airship solar heat protection formed product |
| CN114033322A (en) * | 2021-10-14 | 2022-02-11 | 中海石油(中国)有限公司 | Deepwater oil and gas drilling and carbon dioxide utilization and sequestration integrated device and method |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113378495A (en) * | 2021-07-07 | 2021-09-10 | 中国石油化工股份有限公司 | Composite thermal fluid component prediction system and method |
Family Cites Families (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100024651A1 (en) * | 2008-07-30 | 2010-02-04 | General Electric Company | Membrane contactor systems for gas-liquid contact |
| US20100224062A1 (en) * | 2009-03-05 | 2010-09-09 | Ronald Patterson | Caustic-assisted seawater scrubber system |
| NO330123B1 (en) * | 2009-07-11 | 2011-02-21 | Sargas As | Low CO2 plant for oil sand extraction |
| CN203291707U (en) * | 2013-06-16 | 2013-11-20 | 江苏海事职业技术学院 | Seawater desulfurization system suitable for sulphur waste gas treatment of large and medium-sized ship diesel engine |
| CN203394485U (en) * | 2013-07-12 | 2014-01-15 | 中国石油天然气股份有限公司 | Device for carrying out heavy oil thermal recovery by utilizing boiler flue gas |
| CN103590788A (en) * | 2013-11-19 | 2014-02-19 | 中国海洋石油总公司 | Multielement thermal fluid oil production technology with adjustable components |
| CN104258708A (en) * | 2014-09-25 | 2015-01-07 | 西安华陆环保设备有限公司 | Method for removing SO2 in flue gas by hollow fiber membrane |
| CN104437084B (en) * | 2014-12-10 | 2023-10-31 | 上海亨远船舶设备有限公司 | Desulfurization and denitrification method for tail gas of marine internal combustion engine |
| CN105148728A (en) * | 2015-10-18 | 2015-12-16 | 北京化工大学 | Tail-gas desulfurization system and technique for seawater and fresh water dual-purpose ship |
| CN105417675B (en) * | 2015-12-09 | 2018-01-19 | 大唐环境产业集团股份有限公司 | A kind of desulfurization restoring sea water device and restoration methods based on pure oxygen aeration |
| CN105688687B (en) * | 2016-02-29 | 2018-09-04 | 江苏久朗高科技股份有限公司 | The preparation process of double-hydropholic film |
| CN106076072A (en) * | 2016-07-19 | 2016-11-09 | 江苏优拿大环保科技有限公司 | A kind of ceramic membrane air washer peculiar to vessel and application thereof |
| CN106345197A (en) * | 2016-08-29 | 2017-01-25 | 北京康孚科技股份有限公司 | Metal fibrofelt and corrugated cylinder air filter |
-
2017
- 2017-12-28 CN CN201711464557.0A patent/CN108261899A/en active Pending
-
2018
- 2018-12-28 CN CN201811629572.0A patent/CN109464888A/en active Pending
- 2018-12-28 CN CN201811629658.3A patent/CN109464889A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110026405A (en) * | 2019-04-04 | 2019-07-19 | 北京卫星制造厂有限公司 | A kind of waste gas and waste liquid reclaimer based on recoverable airship solar heat protection formed product |
| CN114033322A (en) * | 2021-10-14 | 2022-02-11 | 中海石油(中国)有限公司 | Deepwater oil and gas drilling and carbon dioxide utilization and sequestration integrated device and method |
| CN114033322B (en) * | 2021-10-14 | 2023-09-22 | 中海石油(中国)有限公司 | Device and method for integrating deep water oil gas drilling and carbon dioxide utilization and sealing |
Also Published As
| Publication number | Publication date |
|---|---|
| CN109464889A (en) | 2019-03-15 |
| CN109464888A (en) | 2019-03-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108261899A (en) | For the equipment of offshore production platform exhuast gas desulfurization and carbon dioxide recovery recharge | |
| CN105129817B (en) | Flue gas SCR denitration urea catalytic hydrolysis ammonia production system and method | |
| CN103611377A (en) | Gas purification pretreatment method and device | |
| CN102690689B (en) | Device and method for scrubbing and purifying coal gas | |
| CN208553653U (en) | A kind of Horizental showering tower for pickling exhaust-gas treatment | |
| CN108300519B (en) | Tar-containing gas generating and purifying device and control method thereof | |
| CN205172695U (en) | Automobile emission purification device | |
| CN209714718U (en) | A kind of new exhuast gas desulfurization equipment | |
| CN209745751U (en) | Sulfur-tolerant methanation catalyst evaluation device | |
| CN205003131U (en) | Integration hydrogen concentration monitoring devices | |
| CN206778150U (en) | Paper mill waste gas purification apparatus | |
| CN214862419U (en) | Blowing gas ammonia desulfurization system | |
| CN211035725U (en) | Total potassium measurement system of barren solution | |
| CN204051384U (en) | A kind of ammonia washing recovering device | |
| CN208389759U (en) | A kind of low-temperature flue gas ozone denitration high efficiency reactor | |
| CN209237671U (en) | A kind of wet desulphurization device for Biogas Generator Set | |
| CN208082148U (en) | A kind of chloropropyl alcohol acidic tail gas absorbing device | |
| CN207259164U (en) | A kind of revolving bed ammonia recovery unit | |
| CN202595069U (en) | Coal gas scrubbing and purifying device | |
| CN208799958U (en) | A kind of horizontal calcium method desulfurizing tower | |
| CN206082089U (en) | Electroplate white fog improve in dedicated high efficiency with refrigerated scrubbing tower | |
| CN205003009U (en) | Cis -butenedioic anhydride on line analyzer tail gas sample preprocessing device | |
| CN220788660U (en) | Spray cooling tower for dedusting converter flue gas | |
| CN210544354U (en) | Alkali liquor injection system | |
| CN207941368U (en) | A kind of carbonization tail gas ammonia-cleaning tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20180710 |