CN206793332U - A kind of organic gas reclaims TRT - Google Patents
A kind of organic gas reclaims TRT Download PDFInfo
- Publication number
- CN206793332U CN206793332U CN201720256347.1U CN201720256347U CN206793332U CN 206793332 U CN206793332 U CN 206793332U CN 201720256347 U CN201720256347 U CN 201720256347U CN 206793332 U CN206793332 U CN 206793332U
- Authority
- CN
- China
- Prior art keywords
- fuel cell
- charcoal canister
- magnetic valve
- air
- voc
- 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.)
- Expired - Fee Related
Links
Landscapes
- Fuel Cell (AREA)
Abstract
Organic gas provided by the utility model reclaims TRT, including collecting hood, drying chamber, charcoal canister one, charcoal canister two and solid fuel cell group, charcoal canister one and charcoal canister two are passed through solid fuel cell group after being desorbed by vavuum pump, incoming air conduit is provided with solid fuel cell group, VOC on-line monitoring mechanisms one and VOC on-line monitorings mechanism two are provided with charcoal canister one and charcoal canister two, VOC monitors mechanism one on-line and VOC on-line monitorings mechanism two controls desorption organic gas in time, waste water and gas delivery pipe is provided below in solid fuel cell group.Described device, by caused organic exhaust gas enrichment in Petroleum Production, processing and transportation, recycled using fuel cell power generation, the supplement recovery electric power in the environment of low concentration, save cost recovery, external output power, turns waste into wealth in the exhaust environment of high concentration, has wide applicability in petrochemical industry.
Description
Technical field
This practicality relates generally to petrochemical industry equipment technology field, specifically, the utility model is related to petrochemical industry and gives up
Flash Gas Compression Skid System field.
Background technology
Volatile organic matter(VOC)Atmospheric photochemical reaction is participated in, secondary organic aerosol can be formed, it may be possible to haze
One of main source, people stays in for a long time also easily induces the diseases such as leukaemia in the higher environment of VOC content.Oil Generation
Production, refining, transport are important VOC anthropogenic discharges sources, and the VOC of discharge not only pollutes atmospheric environment, also causes refining losses.
But VOC emission amount is not fixed, composition is also complex, and waste gas caused by petroleum refining process is adopted mostly at present
With condensation, absorption and sorption, burning and combinations thereof handling process, but operating cost remains high, and is difficult to stably reaching standard discharge,
Also do not recycled.Torch burning, or simple suction are carried out to tidal air caused by Petroleum Production transportation and Volatile Gas
Discharged after attached processing, discharge gas hydro carbons concentration is difficult to up to standard.
The content of the invention
It is high for caused exhaust-gas treatment cost in existing Petroleum Production, processing, transportation, it is impossible to the skill effectively utilized
Art present situation, the utility model provide a kind of organic gas recovery TRT, are handled by adsorption-desorption, it is dense to improve waste gas
Degree, is passed into the generating of solid fuel cell group, and electricity returns to the whole processing procedure of driving once more so that exhaust-gas treatment into
This reduction, caused high-concentration waste gas electricity can also provide production process use in process of oil production, in oil
Work field has wide applicability.
To achieve these goals, the utility model provides a kind of technical scheme:
A kind of organic gas recovery TRT provided by the utility model, including collecting hood, drying chamber, charcoal canister
First, charcoal canister two and solid fuel cell group, air blower one are provided with above collecting hood, air blower one and drying chamber pass through pipe
Road is connected, and drying chamber is connected with charcoal canister one by pipeline, and charcoal canister two is connected with charcoal canister one by pipeline, activity
Canister lower end is provided with purification air discharge pipe, and charcoal canister one and charcoal canister two-way piping are connected with vavuum pump, vacuum
Pump out gas port to be connected with solid fuel cell group organic gas entrance, magnetic valve is provided between drying chamber and charcoal canister one
One, be provided with magnetic valve two between charcoal canister one and charcoal canister two, charcoal canister one and charcoal canister two and vavuum pump it
Between be respectively arranged with magnetic valve three and magnetic valve four, purify and be provided with magnetic valve five, solid fuel cell group in air discharge pipe
On be provided with incoming air conduit, air blower two is provided with incoming air conduit, be provided with charcoal canister one VOC on-line monitoring mechanism
One, VOC on-line monitorings mechanism two, VOC on-line monitoring mechanisms one and VOC on-line monitorings mechanism two-way are provided with charcoal canister two
Cross data wire to be connected with magnetic valve one, magnetic valve two, magnetic valve three, magnetic valve four, magnetic valve five, below solid fuel cell group
It is provided with waste water and gas delivery pipe.
In the utility model, air gauge is provided with the pipe between vavuum pump and solid fuel cell group.
In the utility model, magnetic valve six is provided with waste water and gas delivery pipe, magnetic valve six and air gauge are electrically connected with.
In the utility model, multigroup fuel cell plate is provided with solid fuel cell group, fuel cell plate both sides are set
Have electrode, solid electrolyte be provided among fuel cell plate, the side of solid electrolyte four is provided with stomata, be provided with stomata into
Tracheae.
In the utility model, be provided with ceramic ring in air inlet pipe, ceramic ring be located at fuel cell plate air admission hole both sides, in
Between by high-temp glue by air inlet pipe and stomata joint seal.
In the utility model, side that fuel cell plate contacts with organic gas, which is electrically connected, to be formed battery and bears
The side of pole, described fuel cell plate and air contact is electrically connected to form anode.
In the utility model, air inlet pipe is bilayer sleeve, and inner tube is connected with vavuum pump, and outer tube and incoming air conduit connect
Connect, inner tube has passage to be connected with fuel cell plate negative pole side inner chamber, and outer tube has through hole with fuel cell plate other side
Connection.
The beneficial effects of the utility model:
Organic gas provided by the utility model reclaims TRT, will be produced in Petroleum Production, processing and transportation
Organic exhaust gas enrichment, recycled using fuel cell power generation, in the environment of low concentration supplement recovery electric power, save recovery
Cost, external output power, turns waste into wealth in the exhaust environment of high concentration, has extensive be applicable in petrochemical industry
Property.
Brief description of the drawings
Fig. 1 is shown as the utility model structure diagram.
Fig. 2 is shown as the utility model solid fuel cell group structural representation.
Fig. 3 is shown as the utility model fuel cell plate structure schematic diagram.
Fig. 4 is shown as the utility model air feeder structure schematic diagram.
In figures 1-4,1- collecting hoods, 2- drying chambers, 3- charcoal canisters one, 4- charcoal canisters two, 5- solid fuel cells
Group, 6- air blowers one, 7- fuel cell plates, 8- solid electrolytes, 9- stomatas, 10- air inlet pipe, 11- inner tubes, 12- ceramic rings,
13- passages, 14- through holes, 15- magnetic valves one, 16- magnetic valves two, 17- magnetic valves three, 18- magnetic valves four, 19- magnetic valves five,
20- vavuum pumps, 21- waste water and gas delivery pipe, 22- magnetic valves six, 23- air gauges, 24-VOC on-line monitorings mechanism two, 25-VOC
Monitor mechanism one, 26- electrodes, 27- incoming air conduits, 28- air blowers two on-line.
Embodiment
1 to accompanying drawing 4 and embodiment below in conjunction with the accompanying drawings, and specific embodiment of the present utility model is made further to retouch in detail
State, but the utility model device is not limited to following embodiments.
In this practicality, for the ease of description, a kind of organic gas is reclaimed in TRT, the relative position of each part
The description of relation is that with reference to the accompanying drawings 1 Butut mode is described, such as:The position relationships such as upper and lower, left and right are according to attached
Fig. 1 Butut direction determines.
In the utility model, collecting hood(1), air blower, fuel cell plate(7), ceramic ring, magnetic valve, vavuum pump, air pressure
Table, VOC on-line monitorings mechanism are all bought or customized acquisition by market public channel.
To achieve these goals, the utility model provides a kind of technical scheme:
A kind of organic gas recovery TRT provided by the utility model, including collecting hood(1), drying chamber(2), activity
Canister one(3), charcoal canister two(4)With solid fuel cell group(5), collecting hood(1)Air blower one is provided with above(6), drum
Blower fan one(6)And drying chamber(2)Connected by pipeline, drying chamber(2)With charcoal canister one(3)Connected by pipeline, activated carbon
Tank two(4)With charcoal canister one(3)Connected by pipeline, charcoal canister two(4)Lower end is provided with purification air discharge pipe, activity
Canister one(3)With charcoal canister two(4)Pass through pipeline and vavuum pump(20)Connection, vavuum pump(20)Gas outlet and solid fuel electricity
Pond group(5)Organic gas entrance connects, drying chamber(2)With charcoal canister one(3)Between be provided with magnetic valve one(15), activated carbon
Tank one(3)With charcoal canister two(4)Between be provided with magnetic valve two(16), charcoal canister one(3)With charcoal canister two(4)With it is true
Empty pump(20)Between be respectively arranged with magnetic valve three(17)With magnetic valve four(18), purify and be provided with magnetic valve in air discharge pipe
Five(19), solid fuel cell group(5)On be provided with incoming air conduit(27), incoming air conduit(27)On be provided with air blower two
(28), charcoal canister one(3)On be provided with VOC on-line monitoring mechanism one(25), charcoal canister two(4)On to be provided with VOC online
Mechanism for monitoring two(24), VOC on-line monitorings mechanism one(25)Mechanism two is monitored on-line with VOC(24)Pass through data wire and magnetic valve
One(15), magnetic valve two(16), magnetic valve three(17), magnetic valve four(18), magnetic valve five(19)Connection, solid fuel cell group
(5)Waste water and gas delivery pipe is provided below(21).
In the utility model, vavuum pump(20)With solid fuel cell group(5)Between pipeline on be provided with air gauge
(23).
In the utility model, waste water and gas delivery pipe(21)On be provided with magnetic valve six(22), magnetic valve six(22)It is gentle
Press table(23)It is electrically connected with.
In the utility model, solid fuel cell group(5)Inside it is provided with multigroup fuel cell plate(7), fuel cell plate(7)
Both sides are provided with electrode(26), fuel cell plate(7)Centre is provided with solid electrolyte(8), solid electrolyte(8)Four sides are set
There is stomata(9), stomata(9)In be provided with air inlet pipe(10).
In the utility model, air inlet pipe(10)On be provided with ceramic ring(12), ceramic ring(12)It is located at and fuel cell plate
(7)Air admission hole(9)Both sides, it is middle by high-temp glue by air inlet pipe(10)And stomata(9)Joint seal.
In the utility model, fuel cell plate(7)The side contacted with organic gas, which is electrically connected, to form battery
Negative pole, described fuel cell plate(7)It is electrically connected to form anode with the side of air contact.
In the utility model, air inlet pipe(10)For bilayer sleeve, inner tube(11)With vavuum pump(20)Connection, outer tube and
Incoming air conduit(27)Connection, inner tube(11)With fuel cell plate(7)There is passage negative pole side inner chamber(13)Connection, outer tube with
Fuel cell plate(7)Other side has through hole(14)Connection.
In applicable the utility model device, air blower one is opened(6), by the gas in petrochemical industry production environment slowly
Suck collecting hood(1), transfer to drying chamber(2)Dry, by drying chamber(2)In drier silica dehydrator and after adjusting pH value,
Input charcoal canister one(3)Absorption, residual gas is again introduced into charcoal canister two after majority of gas absorption(4)Absorption, absorption
Air after complete purification is arranged into air.When VOC monitors mechanism one on-line(25)Detect charcoal canister one(3)Middle organic gas is dense
After degree reaches certain value, magnetic valve three(17)Open, remaining closed electromagnetic valve, when VOC monitors mechanism two on-line(24)Detection is lived
Property canister two(4)Kind organic vapor concentrations reach magnetic valve four after certain value(18)Open, remaining closed electromagnetic valve, start simultaneously
Vavuum pump(20), the gas vacuum in charcoal canister is desorbed, is pumped into solid fuel cell group(5)Negative pole generates electricity, and this practicality is new
In type, solid fuel cell group(5)The device of whole set procurement can be used, fuel cell plate negative pole preferentially selects porous nickel-YSZ
Electrode, electrode sheet material YSZ materials, fuel cell plate positive electrode Pt electrodes.
Organic gas provided by the utility model reclaims TRT, effectively realizes the recovery profit of organic exhaust gas
With, the cost of organic waste-gas purification processing is reduced, it is as a result simple and reliable, it is easy to maintain.
As described above, you can preferably realize this practicality, the above embodiments are only to of the present utility model preferred real
The mode of applying is described, and not the scope of the utility model is defined, before the utility model design spirit is not departed from
Put, the various modifications and improvement that those of ordinary skill in the art make to the technical solution of the utility model, this all should be fallen into
In the protection domain that utility model determines.
Claims (7)
1. a kind of organic gas reclaims TRT, including collecting hood, drying chamber, charcoal canister one, charcoal canister two and solid
Fuel cell unit, it is characterised in that air blower one is provided with above collecting hood, air blower one is connected with drying chamber by pipeline,
Drying chamber is connected with charcoal canister one by pipeline, and charcoal canister two is connected with charcoal canister one by pipeline, under charcoal canister
End is provided with purification air discharge pipe, and charcoal canister one and charcoal canister two-way piping are connected with vavuum pump, vavuum pump outlet
Mouth is connected with solid fuel cell group organic gas entrance, and magnetic valve one, activated carbon are provided between drying chamber and charcoal canister
Magnetic valve two is provided between tank one and charcoal canister two, is set respectively between charcoal canister one and charcoal canister two and vavuum pump
Have a magnetic valve three and magnetic valve four, purify and be provided with magnetic valve five in air discharge pipe, be provided with solid fuel cell group into
Air hose, air blower two is provided with incoming air conduit, VOC on-line monitorings mechanism one, charcoal canister are provided with charcoal canister one
Be provided with two VOC on-line monitoring mechanism two, VOC on-line monitoring mechanism one and VOC on-line monitoring mechanism two by data wire with
Magnetic valve one, magnetic valve two, magnetic valve three, magnetic valve four, magnetic valve five connect, and waste water is provided below in solid fuel cell group
Exhaust pipe.
A kind of 2. organic gas recovery TRT as claimed in claim 1, it is characterised in that described vavuum pump and solid
Air gauge is provided with pipeline between fuel cell unit.
A kind of 3. organic gas recovery TRT as claimed in claim 1, it is characterised in that the waste water and gas delivery pipe
On be provided with magnetic valve six, magnetic valve six and air gauge are electrically connected with.
A kind of 4. organic gas recovery TRT as claimed in claim 1, it is characterised in that described solid fuel cell
Multigroup fuel cell plate is provided with group, fuel cell plate both sides are provided with electrode, and solid electricity is provided among fuel cell plate
Xie Zhi, the side of solid electrolyte four are provided with stomata, air inlet pipe are provided with stomata.
5. a kind of organic gas recovery TRT as claimed in claim 4, it is characterised in that set in described air inlet pipe
There is ceramic ring, ceramic ring is located at by high-temp glue that air inlet pipe and stomata seam is close with fuel cell plate air admission hole both sides, centre
Envelope.
6. a kind of organic gas recovery TRT as claimed in claim 4, it is characterised in that the fuel cell plate is with having
The side of machine gas contact is electrically connected to form GND, the side electricity of described fuel cell plate and air contact
Property is joined together to form anode.
7. a kind of organic gas recovery TRT as claimed in claim 4, it is characterised in that described air inlet pipe is bilayer
Sleeve pipe, inner tube are connected with vavuum pump, and outer tube connects with incoming air conduit, and inner tube has with fuel cell plate negative pole side inner chamber
Passage connects, and outer tube has through hole to be connected with fuel cell plate other side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720256347.1U CN206793332U (en) | 2017-03-15 | 2017-03-15 | A kind of organic gas reclaims TRT |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720256347.1U CN206793332U (en) | 2017-03-15 | 2017-03-15 | A kind of organic gas reclaims TRT |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206793332U true CN206793332U (en) | 2017-12-26 |
Family
ID=60729873
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720256347.1U Expired - Fee Related CN206793332U (en) | 2017-03-15 | 2017-03-15 | A kind of organic gas reclaims TRT |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206793332U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112652793A (en) * | 2020-12-21 | 2021-04-13 | 清华大学 | Haze power generation device and power generation method |
-
2017
- 2017-03-15 CN CN201720256347.1U patent/CN206793332U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112652793A (en) * | 2020-12-21 | 2021-04-13 | 清华大学 | Haze power generation device and power generation method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN213728521U (en) | Volatile organic contaminated soil treatment greenhouse system | |
CN206793332U (en) | A kind of organic gas reclaims TRT | |
CN108283870B (en) | Plasma waste gas comprehensive treatment device | |
CN113577944A (en) | Cleaning device is collected to impurity in boiler waste gas | |
CN206535372U (en) | New waste gas filtration and adsorption treatment device | |
CN206560771U (en) | A kind of active carbon adsorption device | |
CN206499973U (en) | A kind of lacquer spraying waste gas processing system | |
CN204247022U (en) | The waste gas treatment equipment that biofiltration is integrated with low temperature plasma | |
CN216346304U (en) | High-efficient VOCs catalytic combustion equipment | |
CN207918498U (en) | Negative oxygen ion sterilization system | |
CN110215810A (en) | A kind of VOCs exhaust treatment system and method | |
CN212236604U (en) | Novel high-efficient vacuum desorption system complete set device | |
CN206508752U (en) | A kind of printing machine Volatile organic emissions processing unit | |
TWM550663U (en) | Improved bypass piping of volatile organic waste gas treatment system | |
CN209865766U (en) | Explosion-proof MW-LEP exhaust-gas treatment equipment | |
CN208449005U (en) | A kind of polluted gas high pressure ionization processing unit | |
CN117282212B (en) | Deposition furnace tail gas power generation system and tail gas treatment method | |
CN206500018U (en) | One kind can the efficient exhaust processor of automatic air-intaking exhaust | |
CN220338240U (en) | Novel environment-friendly waste gas purification circulator | |
CN205995273U (en) | A kind of low-temperature plasma exhaust treatment system | |
CN109966872A (en) | A kind of purifying processing device suitable for organic exhaust gas | |
CN206343061U (en) | A kind of ultraviolet photolysis organic waste gas treatment equipment integrated with activated carbon | |
CN104923059A (en) | Phosphine purifying and recycling device and method | |
CN205392129U (en) | Electrochemistry exhaust treatment device | |
CN111298597A (en) | Novel efficient vacuum desorption system complete device and waste gas treatment method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171226 Termination date: 20190315 |