CN109178697A - A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil - Google Patents

A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil Download PDF

Info

Publication number
CN109178697A
CN109178697A CN201810958410.5A CN201810958410A CN109178697A CN 109178697 A CN109178697 A CN 109178697A CN 201810958410 A CN201810958410 A CN 201810958410A CN 109178697 A CN109178697 A CN 109178697A
Authority
CN
China
Prior art keywords
oil
gas
tank
harbour
making machine
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
Application number
CN201810958410.5A
Other languages
Chinese (zh)
Inventor
许国晨
张旭
陈晓勉
倪振玉
吴公益
宋宗旭
张磊
黄海
王刚
师丽雪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sinopec East China Oil and Gas Co Taizhou Oil Production Plant
Original Assignee
Sinopec East China Oil and Gas Co Taizhou Oil Production Plant
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sinopec East China Oil and Gas Co Taizhou Oil Production Plant filed Critical Sinopec East China Oil and Gas Co Taizhou Oil Production Plant
Priority to CN201810958410.5A priority Critical patent/CN109178697A/en
Publication of CN109178697A publication Critical patent/CN109178697A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D90/00Component parts, details or accessories for large containers
    • B65D90/22Safety features
    • B65D90/30Recovery of escaped vapours

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

The invention discloses a kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil, the present invention is by introducing storage tank tank field, water seal arrangement, in the state of keeping each oil storage tank pressure balance, by being recycled to oil storage tank tank deck and harbour oil carrier Volatile Gas, after Volatile Gas filters out air and inert gas by absorption type device for recovering oil and gas, lime set in outlet pipe is separated by separator, it is pressurized into fuel gas compressor, it then cools down by natural gas dryer, finally burns for heating furnace.Harbour is equipped with nitrogen making machine group, inerting oil carrier cargo tank and system pressure balance, it can be achieved that energy conservation, emission reduction, the purpose to reduce environmental pollution, are effectively saved needed for heating equipment fuel of using by oneself in the present invention.

Description

A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil
Technical field
The present invention relates to be related to oil-gas field surface engineering field, and in particular to a kind of multi-purpose station oil tank top gas and harbour Gas recovery system for oil.
Background technique
To handle oil mass more due to entering the station for some oil-gas field surface engineerings, and is closed process with pressure, has in oil a certain amount of Solution gas, live crude is stored in closed oil storage tank, after the operation such as heated, continuous oil inlet, roof volatilize compared with More head space gas, causes emission to be unsatisfactory for environmental protection code requirement, and emission severely exceeds, exists and seriously pollute big compression ring The phenomenon that border, and waste of resource.
Summary of the invention
Oil storage tank tank deck Volatile Gas can be recycled the purpose of the present invention is to provide one kind and loading dock oil carrier volatilizees The gas recovery system for oil of gas recycling avoids exhaust of oil, pollution environment, achievees the effect that higher energy-saving and emission-reduction.
The technical scheme is that a kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil, including successively Nitrogen making machine group outside the station of connection, absorption type device for recovering oil and gas, separator, stand in fuel gas compressor, drier, oil expeller, Storage tank tank field is in parallel with outer nitrogen making machine group of standing, and is equipped with water seal arrangement in parallel, oil removing between storage tank tank field and outer nitrogen making machine group of standing Device is connected to heating furnace,
(1) it stands outer nitrogen making machine group: by the nitrogen making machine tonifying Qi in Inert Tanks pipe-line system;
When crude oil is loaded onto ship, nitrogen is added in charge of oil ship, makes the oxygen-containing gas concentration of oil carrier Volatile Gas collected below 8%;
When crude oil is not loaded onto ship, Volatile Gas supplement or setting downstream pressure 100Pa, with nitrogen making machine tonifying Qi;
(2) absorption type device for recovering oil and gas: mixed oil and gas enters adsorption system and is adsorbed, and air and inert gas are up to standard After discharge;
Wherein, adsorption system includes the structure of two adsorption tanks of A/B composition, and alternately absorption --- parsing --- cleans Process, under normal pressure the oil-gas component in A tank absorption gaseous mixture, after adsorption saturation, system cuts B tank automatically and carries out at absorption Reason, while A tank carries out vacuum analysis, regenerates adsorbent;Oil gas, which is adsorbed, to be left, and is compressed, is dried, cooling down, point Separate out most of water and light oil, light oil.
Further technical solution, the oil storage tank in storage tank tank field are connected by breather valve with safety valve with atmosphere, setting It breathes valve exhaust and superfeed pressure upper lower limit value is 2000Pa/-250Pa, exhaled when pressure inside the tank is greater than breathing valve opening pressure It inhales valve to open, gas in blowdown vessel;Breather valve is automatically opened when gas pressure is less than breathing valve inlet pressure setting value in tank, Cover gas into tank.
Beneficial effects of the present invention:
1, the present invention feeds them into absorption type device for recovering oil and gas by the recycling to head space gas and harbour oil gas, separates Air and inert gas out enter heating furnace after entering back into fuel gas compressor pressurization, for its burning.Oil carrier when solving charge of oil The recycling problem of gas, effective protection surrounding enviroment meet safety in production, construct harmonious relationship between industry and agriculture, realize energy conservation The target that emission reduction, green low-carbon are developed production.
2, pass through " using harbour oil carrier gas as the supplement gas of shipment oil tank " and set " absorption type in recovery system of the present invention Device for recovering oil and gas " separates the technologies such as air and inert gas, and wherein absorption type device for recovering oil and gas integrally uses skid-mounted type knot Structure, each system are fully integrated into sledge block, and scene only needs to dock gas gathering manifold and unit, give equipment distribution.Sledge block is not by It becomes rusty outer steel shell design, not only anti-corrosion but also beautiful.Present invention process is advanced, safe and reliable to operation, each equipment enclosed in this recovery system Circular flow, energy saving are high;Process equipment auto-control degree is high.And use DCS Distributed Control System, overall monitoring Operating parameter state, flow chart Dynamically Announce, fault alarm, trend record show etc. that functions protect production process effectively Barrier.
Detailed description of the invention
Fig. 1 is flow diagram of the present invention.
Specific embodiment
Below by non-limiting embodiment, the present invention is further explained, understands the present invention.
The present invention reduces continent city joint using the oil gas in the loading dock oil carrier of continent city as the supplement gas of shipment oil tank The investment for big tank tonifying Qi process of standing, while being not required to separately build harbour gas recovering device.
As shown in Figure 1, nitrogen making machine group outside the sequentially connected station of the present invention, absorption type device for recovering oil and gas, separator, stand in Fuel gas compressor, drier, oil expeller, oil expeller are connected to heating furnace, and storage tank tank field is in parallel with outer nitrogen making machine group of standing, storage tank Water seal arrangement in parallel is equipped between tank field and outer nitrogen making machine group of standing, water seal arrangement is a kind of setting for guarantee storage tank operational safety It applies, when tank deck atmospheric pressure is more than this value, water seal arrangement pressure release, the safety of protective pot.Wherein, water seal arrangement sets vent pressure 1200~1400Pa;The nominal volume flow of natural gas compressor is 2Nm3/ min, pressure of inspiration(Pi) are 0.2~0.5KPa, exhaust Pressure is 0.3Mpa.
Heating furnace connection to water seal arrangement, is equipped with direct-operated regulator on pipeline, the pressure after determining valve is by pipeline 100Pa。
When crude oil is loaded onto ship, nitrogen is added in charge of oil ship, makes the oxygen-containing gas concentration of oil carrier Volatile Gas collected below 8%;
When crude oil is not loaded onto ship, Volatile Gas supplement or setting downstream pressure 100Pa, with nitrogen making machine group tonifying Qi;Nitrogen making machine Nitrogen output is >=280Nm3/ h, nitrogen purity >=99% processed,
For the lasting reliability service for ensuring gas recovery system for oil, absorption type device for recovering oil and gas uses two adsorption tanks of A/B The structure of composition, alternately absorption --- parsing --- cleaning process, A tank adsorbs the oil gas group in gaseous mixture under normal pressure Point, after adsorption saturation, system cut automatically B tank carry out adsorption treatment, while A tank carry out vacuum analysis, obtain adsorbent Regeneration parses initial stage, and adsorbent lower part is original gas (oxygen-containing tolerance is more), initially enters surge tank, then Vacuum solutions Analysis recycling adsorbed gas, portion supplements nitrogen on the sorbent, and adsorbed gas oxygen content is seldom, and after nitrogen supplement, oxygen concentration declines again, Consideration sets oxygen detection instrument in surge tank and continuously detects, automatic again when oxygen concentration is below 1.8% in surge tank gas Valve opening exhaust, into big tank air extractor system, recycles this Volatile Gas.Therefore, the collection of this Volatile Gas is discontinuous, when gap Between it is shorter.
Adsorbent meeting heat release during adsorbing oil gas, is equipped with temperature sensor, for monitoring activity on adsorption tanks Charcoal adsorption tanks temperature, if any the situation that temperature is excessively high, system will be switched to another tank, while the tank introduces nitrogen and dropped Temperature will start automatically shutdown procedure if necessary and alarm.Adsorbent need to select import brand Special adsorbent, it is ensured that adsorptivity Can, can recovery section methane gas and discharge part carbon dioxide gas.
Absorption type device for recovering oil and gas uses skid-mounted type structure, and each system is fully integrated into sledge block, scene only need by Gas gathering manifold and unit docking, give equipment distribution.Absorption type device for recovering oil and gas handles tolerance >=355Nm3/ h, non-methane total hydrocarbons Removal efficiency reach 95% or more.
By being recycled to oil storage tank tank deck and harbour oil carrier Volatile Gas in the present invention, it is run through absorption type oil gas and returns Receiving apparatus filters out air and inert gas, and Volatile Gas separates lime set in outlet pipe by separator, is pressurized into fuel gas compressor To 0.2-0.3Mpa, then cool down by natural gas dryer to 10-40 DEG C, finally for heating furnace after oil expeller Burning.
By taking the multi-purpose station project implementation of continent city as an example, continent city multi-purpose station reduces about 39.8~64 × 104Nm every year3Big tank volatilization Gas discharge, loading dock reduce about 28.6~38.2 × 104Nm every year3The discharge of oil carrier Volatile Gas;Continent city multi-purpose station adsorbent equipment Non-methane hydrocarbon emission amount is about 8~20g/m3, meet " storage tank farm atmosphere pollutants emission standards " (GB20950-2007) rule Fixed: exhaust of oil mass concentration is less than or equal to 25g/m3Index request, practical exhaust of oil total amount is seldom, about 2.2~ 5.5×104Nm3/ a is arranged " absorption type device for recovering oil and gas " to build 3.2%~5.4% before big tank air extractor, can Concentration of the oxygen in natural gas is reduced, it is safe and reliable to operation.The nitrogen for reducing supplement enters air extractor system, wherein big tank Nitrogen flow is 260Nm when tonifying Qi3/ h, duration about 8h, nitrogen flow is 40Nm after tonifying Qi3/ h, this two parts enter pot Furnace combustion system, while reducing about 6~10Nm3/ h carbon dioxide gas enters boiler combustion system, reduces combustion heat loss about 1.2 ten thousand yuan/year are convenient for boiler combustion, and (nitrogen and carbon dioxide gas are nothing to the amount for reducing into natural gas compressor gas With part), about 4.7 ten thousand yuan/year of power consumption of natural gas compressor motor is reduced, it is overall to reduce about 5.9 ten thousand yuan/year of running cost.
In conclusion harbour is equipped with nitrogen making machine group in the present invention, inerting oil carrier cargo tank and system pressure balance are, it can be achieved that section Energy, emission reduction, the purpose to reduce environmental pollution are effectively saved needed for heating equipment fuel of using by oneself.

Claims (2)

1. nitrogen making machine group, suction outside a kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil, including sequentially connected station Attached formula device for recovering oil and gas, separator, stand in fuel gas compressor, drier, oil expeller, which is characterized in that storage tank tank field with Outer nitrogen making machine group of standing is in parallel, and water seal arrangement in parallel is equipped between storage tank tank field and outer nitrogen making machine group of standing, and oil expeller, which is connected to, to be added Hot stove,
Wherein, it stands outer nitrogen making machine group: by the nitrogen making machine tonifying Qi in Inert Tanks pipe-line system;When crude oil is loaded onto ship, in charge of oil ship Middle addition nitrogen makes the oxygen-containing gas concentration of oil carrier Volatile Gas collected below 8%;When crude oil is not loaded onto ship, Volatile Gas supplement or Downstream pressure 100Pa is set, with nitrogen making machine tonifying Qi;
Absorption type device for recovering oil and gas: mixed oil and gas enters adsorption system and is adsorbed, air and inert gas rear discharge up to standard; Wherein, adsorption system includes the structure of two adsorption tanks of A/B composition, alternately absorption --- parsing --- cleaning process, Under normal pressure A tank absorption gaseous mixture in oil-gas component, after adsorption saturation, system cut automatically B tank carry out adsorption treatment, simultaneously A tank carries out vacuum analysis, regenerates adsorbent;Oil gas, which is adsorbed, to be left, and is compressed, is dried, cooling down, and big portion is isolated Divide water and light oil, light oil.
2. a kind of multi-purpose station oil tank top gas according to claim 1 and harbour gas recovery system for oil, which is characterized in that Oil storage tank in storage tank tank field is connected by breather valve with safety valve with atmosphere, setting breathing valve exhaust and superfeed pressure bound Value is 2000Pa/-250Pa, and when pressure inside the tank is greater than breathing valve opening pressure, breather valve is opened, gas in blowdown vessel;Work as tank Interior gas pressure automatically opens breather valve when being less than breathing valve inlet pressure setting value, and cover gas into tank.
CN201810958410.5A 2018-08-22 2018-08-22 A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil Pending CN109178697A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810958410.5A CN109178697A (en) 2018-08-22 2018-08-22 A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810958410.5A CN109178697A (en) 2018-08-22 2018-08-22 A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil

Publications (1)

Publication Number Publication Date
CN109178697A true CN109178697A (en) 2019-01-11

Family

ID=64918896

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810958410.5A Pending CN109178697A (en) 2018-08-22 2018-08-22 A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil

Country Status (1)

Country Link
CN (1) CN109178697A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110893955A (en) * 2019-11-18 2020-03-20 西安长庆科技工程有限责任公司 Skid-mounted large tank air extraction device and method
CN111846675A (en) * 2020-08-12 2020-10-30 眉山麦克在线设备股份有限公司 Oil gas volatilization inhibition system and method with inert gas protection function
CN111907953A (en) * 2020-08-12 2020-11-10 眉山麦克在线设备股份有限公司 Oil gas volatilization inhibition system and method

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040045625A1 (en) * 2002-09-09 2004-03-11 Gray John M. Tank pressure management system
CN104096379A (en) * 2014-07-11 2014-10-15 海湾环境科技(北京)股份有限公司 High-sulfur crude oil gas recovery system for docks
CN105771538A (en) * 2016-04-28 2016-07-20 张家港市华昌新材料科技有限公司 Storage tank breathing air recycling method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040045625A1 (en) * 2002-09-09 2004-03-11 Gray John M. Tank pressure management system
CN104096379A (en) * 2014-07-11 2014-10-15 海湾环境科技(北京)股份有限公司 High-sulfur crude oil gas recovery system for docks
CN105771538A (en) * 2016-04-28 2016-07-20 张家港市华昌新材料科技有限公司 Storage tank breathing air recycling method

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
宫中昊等: "码头油气回收系统解析", 《环境工程》 *
潘海涛: "油气回收技术在港口油品码头中的应用", 《中国土木工程学会港口工程分会技术交流文集》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110893955A (en) * 2019-11-18 2020-03-20 西安长庆科技工程有限责任公司 Skid-mounted large tank air extraction device and method
CN111846675A (en) * 2020-08-12 2020-10-30 眉山麦克在线设备股份有限公司 Oil gas volatilization inhibition system and method with inert gas protection function
CN111907953A (en) * 2020-08-12 2020-11-10 眉山麦克在线设备股份有限公司 Oil gas volatilization inhibition system and method

Similar Documents

Publication Publication Date Title
CN109178697A (en) A kind of multi-purpose station oil tank top gas and harbour gas recovery system for oil
AU2016378831A1 (en) Method for producing biomethane by purifying biogas from non-hazardous waste storage facilities and facility for implementing the method
CN103285725B (en) Crude oil lading oil gas recovering method
EP2700439B1 (en) System and method for processing greenhouse gases
CN108792336B (en) Autonomous respiration zero-emission system of nitrogen sealed storage tank and treatment method
CN105289194A (en) Crude oil shipping oil and gas recycling method
CN108114573A (en) The collection and purification recovery system and method for a kind of tank area head space gas
CN202226647U (en) Oil gas recovering system for gas station
CN107837642A (en) A kind of petroleum vapor recovery and exhaust treatment system
CA2808942C (en) System and method for producing carbon dioxide
CN101617030A (en) Flammable gas concentration system
CN201737371U (en) Oil-gas recovering device of oil tank
CN113586953A (en) Carbon emission reduction system and method for LNG power ship
CN104548879B (en) A kind of oil plant sour water tank method for treating release gas and device
CN205994912U (en) A kind of automatic fire extinguishing system of absorbent charcoal adsorption tank
US8226744B2 (en) Repressurization of a VSA treating a gas mixture comprising a fuel
CN204952588U (en) Processing system who contains VOCs waste gas
CN110787585A (en) Recovery method of triphen volatile gas
CN105737517A (en) Method and device for purifying oil storage tank discharge gas
CN102911704A (en) Method for comprehensive oil gas recovery
CN209685715U (en) A kind of recycle device of oil field torch gas
CN204865444U (en) Meticulous processing system in vapor recovery system rear end
CN216612513U (en) Oil storage tank top gas and wharf oil gas recovery system of combined station
CN212383452U (en) Oil gas recovery device by organic membrane separation method
CN205461657U (en) Waste gas active carbon adsorption catalysis desorption process units sprays paint

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

Application publication date: 20190111

WD01 Invention patent application deemed withdrawn after publication