CN109185693A - The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel - Google Patents

The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel Download PDF

Info

Publication number
CN109185693A
CN109185693A CN201811063197.8A CN201811063197A CN109185693A CN 109185693 A CN109185693 A CN 109185693A CN 201811063197 A CN201811063197 A CN 201811063197A CN 109185693 A CN109185693 A CN 109185693A
Authority
CN
China
Prior art keywords
lng
bog
low pressure
outlet
gas
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
CN201811063197.8A
Other languages
Chinese (zh)
Inventor
李欣
王怡
周熲
娄春景
蒯晶晶
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.)
Shanghai Waigaoqiao Shipbuilding Co Ltd
Original Assignee
Shanghai Waigaoqiao Shipbuilding Co Ltd
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 Shanghai Waigaoqiao Shipbuilding Co Ltd filed Critical Shanghai Waigaoqiao Shipbuilding Co Ltd
Priority to CN201811063197.8A priority Critical patent/CN109185693A/en
Publication of CN109185693A publication Critical patent/CN109185693A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/02Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63HMARINE PROPULSION OR STEERING
    • B63H21/00Use of propulsion power plant or units on vessels
    • B63H21/20Use of propulsion power plant or units on vessels the vessels being powered by combinations of different types of propulsion units
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/002Details of vessels or of the filling or discharging of vessels for vessels under pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/04Arrangement or mounting of valves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63HMARINE PROPULSION OR STEERING
    • B63H21/00Use of propulsion power plant or units on vessels
    • B63H21/20Use of propulsion power plant or units on vessels the vessels being powered by combinations of different types of propulsion units
    • B63H2021/202Use of propulsion power plant or units on vessels the vessels being powered by combinations of different types of propulsion units of hybrid electric type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/032Hydrocarbons
    • F17C2221/033Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0102Applications for fluid transport or storage on or in the water
    • F17C2270/0105Ships
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T70/00Maritime or waterways transport
    • Y02T70/50Measures to reduce greenhouse gas emissions related to the propulsion system
    • Y02T70/5218Less carbon-intensive fuels, e.g. natural gas, biofuels

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Ocean & Marine Engineering (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The invention discloses a kind of natural gas high-low pressure integrated gas supply systems of large-scale double fuel Power Vessel, including LNG fuel compartment and high and low pressure air supply system;LNG fuel compartment is IMO Type B film cabin.High pressure air feed system is boosted LNG by LNG booster pump, by LNG high pressure gasifier by LNG gasification and heating, provides the combustion gas for meeting marine main engine required pressure, temperature, flow.Low pressure air supply system includes LNG gasification unit and BOG processing unit.LNG gasification unit, by LNG gasification and heating, provides the combustion gas for meeting generator and/or boiler required pressure, temperature, flow by LNG low pressure gasifying device;BOG processing unit is pressurizeed by room temperature BOG compressor, then adjusts temperature by BOG heater and BOG compressor outlet heat exchanger, provides the combustion gas for meeting double fuel engine machine and/or boiler required pressure, temperature, flow.The present invention keeps air supply system simpler reliable.

Description

The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel
Technical field
The present invention relates to a kind of ships using International Maritime Organization (IMO) Type B cabin as liquefied natural gas (LNG) storage cabin With fuel gas feed system, in particular to a kind of high-low pressure integrated gas supply system of large-scale double fuel Power Vessel, the gas supply system System meets the LNG Power Vessel rule and related classification society rule standard of newest IGF rule.
Background technique
Ship can discharge a large amount of NO to atmosphere in combusting heavy oilX、SOX、CO2And PM2.5 particulate matter, some big Type harbour, river and sea area can all form biggish environmental pollution, one of even main pollution sources.This at present to environmental protection It is required that increasingly paying attention to not being consistent.In addition as MARPOL International Convention for the Prevention of Pollution from Ships is increasingly stringenter, and In view of ship flue gas emission provides the implementation of Tier III, new ship and it is some require to take measures in battalion's ship, subtract NO in few tail gasX、SOXAnd the discharge of PM2.5 particulate matter, with meet the requirement of environmental protection.
LNG is increasingly taken seriously as a kind of clean energy resource, and the emission after burning is environmentally friendly, can reduce 30% or more carbon emission and discharged nitrous oxides, 98% or more sulfur oxides emissions and 30% or so fuel cost.Closely Nian Lai, many governments, shipowner use natural gas as ship power fuel in positive trial.
In recent years, in the world protected environment and meet regulation rule requirement driving, need of the whole world to clean energy resource Ask continuous expansion.According to " world prevents ship from causing environmental pollution pact " (MARPOL supplemental provisions VI --- prevent ship air dirty Dye rule) it requires, all ships by emission control region must satisfy the emission request of oxysulfide and nitrogen oxides, this By demand of the stimulation market to the double fuel powered ship for using natural gas Power Vessel and conventional fuel oil significantly.
The 95th session (MSC 95) of International Maritime Organization (IMO) the Maritime Safety committee held on June 12nd, 2015 " using gas or other low-flash fuel ship world securities rule " (hereinafter referred to as " IGF rule ") is passed through, and in 2015 On July 20, in has issued document with MSC.391 (95), and the mandatory term of the rule is in life on January 1 in 2017 at present Effect.The rule is formally issued as ship and has established solid foundation using LNG fuel, the reality of mandatory provisions in the rule It applies, the risk of ship, crewman and environment is preferably minimized, the double effects with " ship is safer " and " protection environment ".Separately The relevant regulation of outer many natural gas Power Vessel shippings, is also gradually improved.The equipment supply chain of the natural pneumatic power system of ship It is complete effective.
The host configured on large-scale double fuel Power Vessel is the ME-GI power team of graceful benefactor department, is two-stroke high pressure Gaseous propellant engine is sprayed, gas supply operating pressure reaches 300bar or so, is known as " high-pressure air feed system for the system of its gas supply System ".The subsidiary engine configured on ship includes gas electricity generator and gas fired-boiler, and gas electricity generator is that four stroke dual-fuel of low pressure starts Machine, supply gas pressure are usually less than 10bar, and by taking the medium-speed engine of watt Ceylon as an example, supply gas pressure is 6bar or so, supply for it The system of gas is known as " low pressure air supply system ".The supply gas pressure of double fuel boiler is not higher than 6bar.For this purpose, needing to consider on ship same The a set of high pressure air feed system of Shi Peibei and low pressure air supply system, to meet the air supply requirement of high pressure host and the gas supply of low pressure subsidiary engine It is required that.Structure is complicated for existing high-low pressure air supply system, and volume is big, and equipment investment is big.
Summary of the invention
A kind of natural gas of large-scale double fuel Power Vessel is provided it is an object of the invention to overcome the deficiencies of existing technologies High-low pressure integrated gas supply system, it solves different demands of the double fuel Power Vessel using multiple types gas equipment to combustion gas, And change the process flow of existing air supply system complexity, keep air supply system simpler reliable.
The object of the present invention is achieved like this: a kind of integrated gas supply system of the natural gas high-low pressure of large size double fuel Power Vessel System, for providing the gas fuel of different pressures, temperature and flow to the gas equipment on ship;The gas equipment includes ship Oceangoing ship host, generator and boiler;The marine main engine uses low speed two-stroke dual-fuel;During the generator and boiler are all made of Fast four stroke dual-fuels;The high-low pressure integrated gas supply system includes LNG fuel compartment, LNG filling station, high pressure air feed system and low Press air supply system;Wherein,
The LNG fuel compartment is IMO Type B film cabin;
The filling station includes the LNG filling pipeline being connected to the LNG fuel compartment and the top for being connected to LNG fuel compartment BOG return duct;
The high pressure air feed system includes the LNG immersed pump being located in the LNG fuel compartment, by LNG delivery pipe and LNG The surge tank of the outlet connection of immersed pump, the outlet of the surge tank are connect with the import of high-pressure air feed pipeline, high-pressure air feed pipeline On LNG booster pump and LNG high pressure gasifier are successively installed, the outlet of the high-pressure air feed pipeline by host combustion gas valve group with it is described Marine main engine connection;LNG highest can be pressurized to 300bar by the LNG booster pump;
The LNG booster pump uses hydraulic-driven and provides power by individual hydraulic power unit for it, this is hydraulic dynamic Power unit arrangement safety zone aboard ship, or the hydraulic system that use marine main engine to carry provided for the LNG booster pump it is dynamic Power;
The low pressure air supply system includes LNG gasification unit and BOG processing unit;
The LNG gasification unit includes the low pressure steam line and be mounted on low pressure air supply pipe that the outlet with surge tank connects LNG low pressure gasifying device on road, the outlet of the low pressure steam line are connect with subsidiary engine combustion gas valve group and boiler flue gas valve group respectively, The subsidiary engine combustion gas valve group and boiler flue gas valve group are connect with the generator and boiler correspondingly;
The BOG processing unit includes the BOG pipeline connecting with the top of the LNG fuel compartment, is mounted on BOG pipeline BOG heater, with BOG heater outlet connection BOG gas-liquid separator, pass through BOG air inlet pipe and BOG gas-liquid separator Gas vent connection BOG compressor, changed by the compressor outlet that BOG exhaust pipe is connect with the gas outlet of BOG compressor Hot device, the outlet of the compressor outlet heat exchanger are connect with subsidiary engine combustion gas valve group and boiler flue gas valve group respectively, the subsidiary engine combustion Air valve group and boiler flue gas valve group are connect with the generator and boiler correspondingly;The BOG heater can be LNG fuel Evaporated natural gas in cabin is warming up to 0 DEG C or more;The BOG compressor is room temperature BOG compressor and can be evaporated natural gas Pressure boost is to being no more than 10bar;The temperature of pressurized evaporated natural gas is heated to 20 by the compressor outlet heat exchanger ~40 DEG C.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein the LNG is high-pressure gasified Device, LNG low pressure gasifying device, BOG heater and compressor outlet heat exchanger by the same Two-way Cycle heating system heats and are adopted Spent glycol aqueous solution is as heat transferring medium;The Two-way Cycle heating system includes glycol water expansion drum and ethylene glycol The sequentially connected glycol water delivery pump of the liquid outlet of aqueous solution expansion drum and glycol water heater, the ethylene glycol The liquid outlet of the aqueous solution heater heat exchanger tube with the import of the heat exchanger tube of LNG high pressure gasifier, LNG low pressure gasifying device respectively Import, the import of heat exchanger tube of BOG heater are connected with the import of the heat exchanger tube of compressor outlet heat exchanger;The LNG high pressure The outlet of the heat exchanger tube of gasifier, the outlet of the heat exchanger tube of LNG low pressure gasifying device, BOG heater heat exchanger tube outlet and pressure The outlet of the heat exchanger tube of contracting machine outlet heat exchanger is connect with the inlet of glycol water expansion drum;The ethylene glycol is water-soluble The steam that liquid heater is generated using the boiler is as heat transferring medium.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein the LNG filling station has Two and respectively it is located at the left and right side of a ship of ship;The BOG return duct on the bank or filling ship connect.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein the LNG immersed pump, LNG booster pump and room temperature BOG compressor configure two, wherein one is spare;When the pressure of LNG fuel compartment is more than setting value When, two room temperature BOG compressors work at the same time.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein the LNG fuel compartment Natural gas vent mast top installation safety valve and connect with safety valve.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein at the generator During the work of combustion gas mode, 0~10kPa is in by the pressure of the BOG compressor control LNG fuel compartment always.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein when the marine main engine It does not work in combustion gas mode with generator or during stopping working, and when the pressure of LNG fuel compartment is close to 70kPa, passes through boiler It is run under combustion gas mode, to consume BOG.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein the host gas valve Group, subsidiary engine combustion gas valve group and boiler flue gas valve group are all made of interlocking valve group and are respectively disposed in an individual combustor.
The natural gas high-low pressure integrated gas supply system of above-mentioned large-scale double fuel Power Vessel, wherein the high-pressure air feed pipe Road and low pressure steam line are all made of double-wall pipe.
The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel of the invention, solves double fuel Power Vessel Using multiple types gas equipment to the different demands of combustion gas, and change the process flow of existing air supply system complexity, makes to supply System is simpler reliable.The present invention also has the following characteristics that
1, perfect BOG Managed Solution: various heating amounts needed for ship are provided by the steam that boiler generates, and can not only be saved The about energy, and extra BOG combustion gas is directly burnt up compared to using gas burner (GCU), double fuel boiler is preferably sharp With the BOG in LNG fuel compartment, it is allowed to be converted into the electric energy that navigation promotes in the process and service is required, on the one hand also fully The energy is utilized, avoids the waste of BOG, BOG accomplishes zero-emission under nominal situation.On the other hand solve LNG fuel compartment because BOG largely gathers the danger for generating hypertonia, delays the rate of pressure rise of LNG fuel compartment significantly, is conducive to control LNG fuel compartment Pressure, extend LNG fuel compartment and hold time, so as to meeting " international using gas or other low-flash fuel ships Safety regulation " (IGF CODE) require 15 days minimal maintenance time.
2, it uses room temperature BOG compressor: comparing cryogenic compressor, normal temperature compressed the had cost performance of machine is very high, tool Have and safeguards simple, the convenient outstanding advantages of starting.
3, LNG booster pump uses the form of hydraulic-driven: compared to the pressurization for using explosion-proof electric machine driving in existing system Pump, has many advantages, such as that equipment occupation space is small, investment of equipment is few, easy to maintenance using the booster pump of hydraulic-driven.Especially The advantage that equipment is compact to design, size is small has special significance to the biggish ship of limited space.
Detailed description of the invention
Fig. 1 is the schematic diagram of the natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel of the invention.
Specific embodiment
The present invention will be further described with reference to the accompanying drawings.
Referring to Fig. 1, the natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel of the invention, for ship On gas equipment provide different pressures, temperature and flow gas fuel;Gas equipment includes marine main engine 21, generator 20 and boiler 19;Marine main engine 1 is using the ME-GI engine of graceful benefactor department, and device is using low speed two-stroke dual-fuel, supply gas pressure 300bar or so, 50 DEG C of feed air temperature;Generator 20 and boiler 19 are all made of four stroke dual-fuel of middling speed, and supply gas pressure 6bar is left The right side, 50 DEG C of feed air temperature.Two kinds of fuel of bunker oil and LNG all can be used in marine main engine 1, generator 20 and boiler 19.
The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel of the invention includes LNG fuel compartment 1;LNG Filling station 3, high pressure air feed system and low pressure air supply system.
LNG fuel compartment 1 uses IMO Type B film cabin, and the design pressure in cabin is 0.7barg, and minimum design temperature is -163 ℃.The natural gas vent mast 6 that the top of LNG fuel compartment 1 is installed safety valve and connect with safety valve.
LNG filling station 3 includes the LNG filling pipeline 5 being connected to LNG fuel compartment 1 and the top for being connected to LNG fuel compartment 1 BOG return duct 4;There are two LNG filling stations 3 and is respectively located at the left and right side of a ship of ship;When LNG is filled, pass through LNG filler pipe Road 5 is directly injected into LNG fuel compartment 1, while BOG is returned on the bank or filled ship by BOG return duct 4.
High pressure air feed system includes the LNG immersed pump 2 being located in LNG fuel compartment 1, by LNG delivery pipe and LNG immersed pump The surge tank 11 of 2 outlet connection, the outlet of the surge tank 11 are connect with the import of high-pressure air feed pipeline 24, high-pressure air feed pipeline LNG booster pump 22 and LNG high pressure gasifier 8 are successively installed, the outlet of the high-pressure air feed pipeline 24 passes through host gas valve on 24 Group 15 is connect with marine main engine 21.LNG booster pump 22 uses hydraulic-driven and is provided by individual hydraulic power unit for it dynamic Power, or the hydraulic system for using marine main engine 1 included provide power for LNG booster pump 22.
The gas supply principle of high pressure air feed system is: LNG immersed pump 2 out of LNG fuel compartment 1 is extracted LNG out, is pressed and delivered to In surge tank 11, the design pressure of surge tank 11 is 10barg;LNG, which enters LNG booster pump 22 from the outlet of surge tank 11, to carry out Boosting, can be pressurized to 300bar for LNG highest, the gasification of LNG high pressure gasifier Final 8's system and heating are then sent to, after making gasification Natural gas meet the combustion requirements of the needs of marine main engine 1, then flow to high-pressure air feed pipeline 24 and by host combustion gas valve group 15 use to the consumption of marine main engine 21.
Low pressure air supply system includes LNG gasification unit and BOG (evaporated natural gas) processing unit;Wherein:
LNG gasification unit includes the low pressure steam line 25 and be mounted on low pressure air supply pipe that the outlet with surge tank 11 connects LNG low pressure gasifying device 12 on road 25, the outlet of the low pressure steam line 25 respectively with subsidiary engine combustion gas valve group 13 and boiler flue gas Valve group 14 connects, and subsidiary engine combustion gas valve group 13 and boiler flue gas valve group 14 are connect with generator 19 and boiler 20 correspondingly;LNG Low pressure gasifying device 12 can be by LNG forced gasification and heating, and the natural gas after making gasification meets what generator 19 and boiler 20 needed Combustion requirements then flow to low pressure steam line 25, further depressurize respectively and transmission & distribution to subsidiary engine combustion gas valve group 13 and boiler Combustion gas valve group 14, is provided to generator 19 and the consumption of boiler 20 uses.
BOG processing unit includes the BOG pipeline 26 connecting with the top of LNG fuel compartment 1, is mounted on BOG pipeline 26 The BOG gas-liquid separator 9 of the outlet connection of BOG heater 7 and BOG heater 7 is divided by BOG air inlet pipe 27 and BOG gas-liquid The BOG compressor 10 of gas vent connection from device 9, the pressure being connect by BOG exhaust pipe 28 with the gas outlet of BOG compressor 10 Contracting machine export heat exchanger 23, the outlet of the compressor outlet heat exchanger 23 respectively with subsidiary engine combustion gas valve group 13 and boiler flue gas valve group 14 connections, subsidiary engine combustion gas valve group 13 and boiler flue gas valve group 14 are connect with generator 19 and boiler 20 correspondingly.
The course of work of BOG processing unit is: the low temperature BOG in LNG fuel compartment 1 first passes through BOG heater 7 and heats up To 0 DEG C or more, BOG gas-liquid separator 9 is subsequently entered, the BOG come out from 9 gas vent of BOG gas-liquid separator is again by room temperature BOG Compressor 10 is pressurized, pressurized gaseous-pressure not more than 10barg, and combustion gas passes through compressor outlet heat exchanger 23 Heating, is heated to 20~40 DEG C, then further respectively decompression and transmission & distribution to subsidiary engine combustion gas valve group 13 and boiler flue gas valve group 14, It is finally provided to generator 19 and the consumption of boiler 20 uses.
LNG high pressure gasifier 8, LNG low pressure gasifying device 12, BOG heater 7 and compressor outlet heat exchanger 23 are by same A Two-way Cycle heating system heats simultaneously use glycol water as heat transferring medium, avoid equipment corrosion and scaling and icing;It is double Loop heating system includes glycol water expansion drum 16, sequentially connected with the liquid outlet of glycol water expansion drum 16 Glycol water delivery pump 18 and glycol water heater 17, the 17 liquid outlets difference of the glycol water heater The import of the heat exchanger tube of import, LNG low pressure gasifying device 12 with the heat exchanger tube of LNG high pressure gasifier 8, the heat exchange of BOG heater 7 The import of pipe is connected with the import of the heat exchanger tube of compressor outlet heat exchanger 23;The outlet of the heat exchanger tube of LNG high pressure gasifier 8, The outlet of the heat exchanger tube of LNG low pressure gasifying device 12, the outlet of the heat exchanger tube of BOG heater 7 and compressor outlet heat exchanger 23 The outlet of heat exchanger tube is connect with the inlet of glycol water expansion drum 16;Glycol water heater 17 uses boiler 20 steam generated are as heat transferring medium.
The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel of the invention has the following characteristics that
1) LNG in LNG fuel compartment 1 pumps 22 conveying and pressurization by LNG immersed pump 2 and LNG hydraulic booster, then passes through LNG high pressure gasifier 8 and LNG low pressure gasifying device 12 are gasified and are heated up, and are provided and are met double fuel marine main engine 21, double fuel The combustion gas of generator 19 and/or double fuel boiler 20 required pressure, temperature, flow;
2) BOG in LNG fuel compartment 1 is pressurizeed by room temperature BOG compressor 10, then by BOG heater 7 and BOG compressor It exports heat exchanger 23 and adjusts temperature, the combustion for meeting double fuel engine machine 19 and/or boiler required pressure, temperature, flow is provided Gas;
3) according to the requirement of IGF rule and classification society rule, the LNG being arranged between air supply system and gas equipment is conveyed Pipe, high-pressure air feed pipeline 24, low pressure steam line 25, BOG pipeline 26, BOG air inlet pipe 27 and BOG exhaust pipe 28 are all made of double-walled Pipe, and host combustion gas valve group 15, subsidiary engine combustion gas valve group 13 and boiler flue gas valve group 14 are respectively disposed at individual combustor (GVU) it in, supplies for separating gas in time and prevents gas leakage from spreading;Host combustion gas valve group 15, subsidiary engine combustion gas valve group 13 Interlocking valve group is all made of with boiler flue gas valve group 14;
4) two LNG immersed pumps 2 of system configuration, LNG booster pump 22 and room temperature BOG compressor 10, when wherein a pump is sent out Another work can be started when raw failure;
5) when double fuel engine machine 19 combustion gas mode work during, pass through room temperature BOG compressor 10 control LNG fuel compartment 1 pressure is in the pressure between 0~10kPa always;When marine main engine 21 and generator 19 do not work or stop in combustion gas mode During only working, and when the pressure of LNG fuel compartment 1 is close to 70kPa, run under combustion gas mode by boiler 20, to consume BOG To maintain to be greater than for a long time 15 days LNG fuel compartments 1 not boost (requirement of IGF rule), or even slowly decompression;
6) during LNG filling, room temperature BOG compressor 10 can be forced to convey BOG into the function of being back on the bank or fill ship; Or two room temperature BOG compressors 10 work at the same time, pressure send extra BOG to double fuel engine machine and/or double fuel pot Furnace consumes;
7) when the hypertonia of LNG fuel compartment or other special operation conditions, two room temperature BOG compressors 10 can work simultaneously Make, making BOG treating capacity is more than one times of the evaporation capacity of LNG fuel compartment 1 or even several times or more, so as to quickly and effectively reduce The pressure of LNG fuel compartment 1;
8) in normal conditions, the natural gas of 24 superpressure of general high voltage steam line discharge can return to low pressure LNG surge tank In 13, the natural gas of 25 superpressure of low pressure steam line discharge be can return in LNG fuel compartment 1, avoid the waste of natural gas and to ring The pollution in border;
9) under emergency work condition, LNG pipe-line system and relevant device (non-LNG fuel compartment) have dump natural gas extremely It is vented the function of mast 6;
10) under emergency work condition, and in authorized situation, the emergency blow-down valve of LNG fuel compartment 1 can be opened manually, Direct cold discharge boil-off gas extremely emptying mast 6;
11) when the setting value that the pressure of LNG fuel compartment 1 is more than safety valve, the peace of any one or more LNG fuel compartment 1 Full valve can discharge in time boil-off gas and control the pressure of LNG fuel compartment 1.
12) when LNG booster pump 22, which configures individual hydraulic power unit, provides power for it, hydraulic power unit can cloth Safety zone aboard ship is set, requirement of explosion proof is not necessarily to.The design of LNG booster pump need to follow the specification and related guidance of marine main engine File.
Above embodiments are used for illustrative purposes only, rather than limitation of the present invention, the technology people in relation to technical field Member, without departing from the spirit and scope of the present invention, can also make various transformation or modification, therefore all equivalent Technical solution also should belong to scope of the invention, should be limited by each claim.

Claims (9)

1. a kind of natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel, for being provided to the gas equipment on ship The gas fuel of different pressures, temperature and flow;The gas equipment includes marine main engine, generator and boiler;The ship Oceangoing ship host uses low speed two-stroke dual-fuel;The generator and boiler are all made of four stroke dual-fuel of middling speed;The high-low pressure Integrated gas supply system includes LNG fuel compartment, LNG filling station, high pressure air feed system and low pressure air supply system;It is characterized in that,
The LNG fuel compartment is IMO Type B film cabin;
The filling station includes the LNG filling pipeline being connected to the LNG fuel compartment and the top for being connected to LNG fuel compartment BOG return duct;
The high pressure air feed system includes the LNG immersed pump being located in the LNG fuel compartment, liquid of being dived by LNG delivery pipe and LNG The surge tank of the outlet connection of pump, the outlet of the surge tank connect with the import of high-pressure air feed pipeline, on high-pressure air feed pipeline according to The outlet of secondary installation LNG booster pump and LNG high pressure gasifier, the high-pressure air feed pipeline passes through host combustion gas valve group and the ship Host connection;LNG highest can be pressurized to 300bar by the LNG booster pump;
The LNG booster pump uses hydraulic-driven and provides power by individual hydraulic power unit for it, the hydraulic power list The safety zone of member arrangement aboard ship, or the hydraulic system for using marine main engine included provide power for the LNG booster pump;
The low pressure air supply system includes LNG gasification unit and BOG processing unit;
The LNG gasification unit includes the low pressure steam line and be mounted on low pressure steam line that the outlet with surge tank connects LNG low pressure gasifying device, the outlet of the low pressure steam line is connect with subsidiary engine combustion gas valve group and boiler flue gas valve group respectively, described Subsidiary engine combustion gas valve group and boiler flue gas valve group are connect with the generator and boiler correspondingly;
The BOG processing unit includes the BOG pipeline connecting with the top of the LNG fuel compartment, is mounted on BOG pipeline The BOG gas-liquid separator of the outlet connection of BOG heater and BOG heater passes through BOG air inlet pipe and BOG gas-liquid separator The BOG compressor of gas vent connection is exchanged heat by the compressor outlet that BOG exhaust pipe is connect with the gas outlet of BOG compressor Device, the outlet of the compressor outlet heat exchanger are connect with subsidiary engine combustion gas valve group and boiler flue gas valve group respectively, the subsidiary engine combustion gas Valve group and boiler flue gas valve group are connect with the generator and boiler correspondingly;The BOG heater can be LNG fuel compartment Interior evaporated natural gas is warming up to 0 DEG C or more;The BOG compressor is room temperature BOG compressor and can be the pressure of evaporated natural gas Power is pressurized to no more than 10bar;The temperature of pressurized evaporated natural gas is heated to 20 by the compressor outlet heat exchanger~ 40℃。
2. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In the LNG high pressure gasifier, LNG low pressure gasifying device, BOG heater and compressor outlet heat exchanger are followed by same pair Ring heating system heats simultaneously use glycol water as heat transferring medium;The Two-way Cycle heating system includes that ethylene glycol is water-soluble It is liquid expansion drum, water-soluble with the sequentially connected glycol water delivery pump of liquid outlet and ethylene glycol of glycol water expansion drum Liquid heater, the liquid outlet of the glycol water heater are low with the import of the heat exchanger tube of LNG high pressure gasifier, LNG respectively Press the heat exchanger tube of the import of heat exchanger tube of gasifier, the import of the heat exchanger tube of BOG heater and compressor outlet heat exchanger into Mouth connection;The outlet of the heat exchanger tube of the LNG high pressure gasifier, the outlet of the heat exchanger tube of LNG low pressure gasifying device, BOG heater Heat exchanger tube outlet and compressor outlet heat exchanger heat exchanger tube inlet of the outlet with glycol water expansion drum Connection;The steam that the glycol water heater is generated using the boiler is as heat transferring medium.
3. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In there are two the LNG filling stations and is respectively located at the left and right side of a ship of ship;The BOG return duct on the bank or filling ship connect It connects.
4. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In the LNG immersed pump, LNG booster pump and room temperature BOG compressor configure two, wherein one is spare;When LNG fuel When the pressure in cabin is more than setting value, two room temperature BOG compressors are worked at the same time.
5. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In the natural gas vent mast that the top of the LNG fuel compartment is installed safety valve and connect with safety valve.
6. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist During the generator is in the work of combustion gas mode, always by the pressure of the BOG compressor control LNG fuel compartment In 0~10kPa.
7. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In when the marine main engine and generator be not during combustion gas mode works or stops working, and the pressure of LNG fuel compartment is close When 70kPa, run under combustion gas mode by boiler, to consume BOG.
8. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In the host combustion gas valve group, subsidiary engine combustion gas valve group and boiler flue gas valve group are all made of interlocking valve group and are respectively disposed at one In individual combustor.
9. the natural gas high-low pressure integrated gas supply system of large size double fuel Power Vessel according to claim 1, feature exist In the high-pressure air feed pipeline and low pressure steam line are all made of double-wall pipe.
CN201811063197.8A 2018-09-12 2018-09-12 The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel Pending CN109185693A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811063197.8A CN109185693A (en) 2018-09-12 2018-09-12 The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811063197.8A CN109185693A (en) 2018-09-12 2018-09-12 The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel

Publications (1)

Publication Number Publication Date
CN109185693A true CN109185693A (en) 2019-01-11

Family

ID=64910668

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811063197.8A Pending CN109185693A (en) 2018-09-12 2018-09-12 The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel

Country Status (1)

Country Link
CN (1) CN109185693A (en)

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109812357A (en) * 2019-01-25 2019-05-28 太平洋海洋工程(舟山)有限公司 A kind of diesel oil and natural gas double-fuel electricity generation system
CN110371246A (en) * 2019-07-18 2019-10-25 上海外高桥造船有限公司 Double fuel super-container vessel air supply system and super-container vessel
CN110748439A (en) * 2019-10-16 2020-02-04 大连船舶重工集团有限公司 Low-pressure gas supply system capable of efficiently utilizing cold energy of LNG (liquefied natural gas) fuel
CN111306438A (en) * 2020-03-24 2020-06-19 江苏科技大学 Gasification device of double-fuel machine LNG high-low pressure gas supply system
CN111609311A (en) * 2020-05-27 2020-09-01 青岛双瑞海洋环境工程股份有限公司 Low-pressure LNG (liquefied Natural gas) supply system of dual-fuel ship engine and dual-fuel ship
CN112498648A (en) * 2020-11-27 2021-03-16 沪东中华造船(集团)有限公司 LNG transport ship volatile gas recycling energy storage system
CN113734352A (en) * 2021-09-24 2021-12-03 上海外高桥造船有限公司 Gas supply system with re-condensation function and working method
CN113958875A (en) * 2021-10-20 2022-01-21 中国船舶重工集团柴油机有限公司 High-pressure fuel gas supply system and method for ship
CN114109659A (en) * 2021-11-26 2022-03-01 招商局重工(深圳)有限公司 LPG fuel pipeline control method
CN114179991A (en) * 2021-11-18 2022-03-15 上海江南长兴造船有限责任公司 Load test method for fuel gas supply system of dual-fuel container ship
CN114379715A (en) * 2021-12-06 2022-04-22 沪东中华造船(集团)有限公司 Ship cabin pressure control system
CN114412635A (en) * 2021-12-06 2022-04-29 沪东中华造船(集团)有限公司 Volatile gas comprehensive management system for fuel power generation device
CN114458950A (en) * 2021-12-29 2022-05-10 长江三星能源科技股份有限公司 Integrated compact LNG gas supply system gasification sled dress equipment
CN114592990A (en) * 2022-03-23 2022-06-07 嘉兴亚航信息技术有限公司 LNG dual-fuel power ship gas supply system
CN114754289A (en) * 2022-05-07 2022-07-15 威海中远海运重工科技有限公司 LNG ship low-pressure gas supply system and method

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20130035058A (en) * 2011-09-29 2013-04-08 삼성중공업 주식회사 System and method for fuel gas supply
KR101277833B1 (en) * 2013-03-06 2013-06-21 현대중공업 주식회사 A fuel gas supply system of liquefied natural gas
CN104265512A (en) * 2014-09-17 2015-01-07 刘国满 High-pressure/low-pressure gas supply system of ship power plant
CN104276270A (en) * 2013-07-24 2015-01-14 中远船务工程集团有限公司 LNG (Liquefied Natural Gas) storage tank arrangement system and gas supply arrangement system of double-fuel power-propelled ship
CN104534277A (en) * 2014-10-29 2015-04-22 沪东重机有限公司 Gas supply system and method for outputting high-pressure gas and low-pressure gas simultaneously
CN105745427A (en) * 2013-11-07 2016-07-06 大宇造船海洋株式会社 Apparatus and method for supplying fuel to engine of ship
CN206346844U (en) * 2016-11-26 2017-07-21 东莞市新奥车用燃气发展有限公司 LNG composite air supplies system peculiar to vessel
CN107339611A (en) * 2017-08-25 2017-11-10 成都华气厚普机电设备股份有限公司 A kind of seagoing vessel LNG fuel low pressure air supply systems and its control method
CN207094185U (en) * 2017-08-25 2018-03-13 成都华气厚普机电设备股份有限公司 A kind of seagoing vessel LNG fuel high pressure air supply systems

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20130035058A (en) * 2011-09-29 2013-04-08 삼성중공업 주식회사 System and method for fuel gas supply
KR101277833B1 (en) * 2013-03-06 2013-06-21 현대중공업 주식회사 A fuel gas supply system of liquefied natural gas
CN104276270A (en) * 2013-07-24 2015-01-14 中远船务工程集团有限公司 LNG (Liquefied Natural Gas) storage tank arrangement system and gas supply arrangement system of double-fuel power-propelled ship
CN105745427A (en) * 2013-11-07 2016-07-06 大宇造船海洋株式会社 Apparatus and method for supplying fuel to engine of ship
CN104265512A (en) * 2014-09-17 2015-01-07 刘国满 High-pressure/low-pressure gas supply system of ship power plant
CN104534277A (en) * 2014-10-29 2015-04-22 沪东重机有限公司 Gas supply system and method for outputting high-pressure gas and low-pressure gas simultaneously
CN206346844U (en) * 2016-11-26 2017-07-21 东莞市新奥车用燃气发展有限公司 LNG composite air supplies system peculiar to vessel
CN107339611A (en) * 2017-08-25 2017-11-10 成都华气厚普机电设备股份有限公司 A kind of seagoing vessel LNG fuel low pressure air supply systems and its control method
CN207094185U (en) * 2017-08-25 2018-03-13 成都华气厚普机电设备股份有限公司 A kind of seagoing vessel LNG fuel high pressure air supply systems

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109812357B (en) * 2019-01-25 2020-08-18 太平洋海洋工程(舟山)有限公司 Diesel oil and natural gas dual-fuel power generation system
CN109812357A (en) * 2019-01-25 2019-05-28 太平洋海洋工程(舟山)有限公司 A kind of diesel oil and natural gas double-fuel electricity generation system
CN110371246A (en) * 2019-07-18 2019-10-25 上海外高桥造船有限公司 Double fuel super-container vessel air supply system and super-container vessel
CN110371246B (en) * 2019-07-18 2022-02-01 上海外高桥造船有限公司 Dual-fuel ultra-large container ship gas supply system and ultra-large container ship
CN110748439A (en) * 2019-10-16 2020-02-04 大连船舶重工集团有限公司 Low-pressure gas supply system capable of efficiently utilizing cold energy of LNG (liquefied natural gas) fuel
CN111306438B (en) * 2020-03-24 2021-09-07 江苏科技大学 Gasification device of double-fuel machine LNG high-low pressure gas supply system
CN111306438A (en) * 2020-03-24 2020-06-19 江苏科技大学 Gasification device of double-fuel machine LNG high-low pressure gas supply system
CN111609311A (en) * 2020-05-27 2020-09-01 青岛双瑞海洋环境工程股份有限公司 Low-pressure LNG (liquefied Natural gas) supply system of dual-fuel ship engine and dual-fuel ship
CN112498648A (en) * 2020-11-27 2021-03-16 沪东中华造船(集团)有限公司 LNG transport ship volatile gas recycling energy storage system
CN113734352A (en) * 2021-09-24 2021-12-03 上海外高桥造船有限公司 Gas supply system with re-condensation function and working method
CN113958875A (en) * 2021-10-20 2022-01-21 中国船舶重工集团柴油机有限公司 High-pressure fuel gas supply system and method for ship
CN114179991A (en) * 2021-11-18 2022-03-15 上海江南长兴造船有限责任公司 Load test method for fuel gas supply system of dual-fuel container ship
CN114179991B (en) * 2021-11-18 2023-11-17 上海江南长兴造船有限责任公司 Load test method for fuel gas supply system of dual-fuel container ship
CN114109659A (en) * 2021-11-26 2022-03-01 招商局重工(深圳)有限公司 LPG fuel pipeline control method
CN114379715A (en) * 2021-12-06 2022-04-22 沪东中华造船(集团)有限公司 Ship cabin pressure control system
CN114412635A (en) * 2021-12-06 2022-04-29 沪东中华造船(集团)有限公司 Volatile gas comprehensive management system for fuel power generation device
CN114412635B (en) * 2021-12-06 2024-04-09 沪东中华造船(集团)有限公司 Volatile gas integrated management system for fuel power generation device
CN114458950A (en) * 2021-12-29 2022-05-10 长江三星能源科技股份有限公司 Integrated compact LNG gas supply system gasification sled dress equipment
CN114592990A (en) * 2022-03-23 2022-06-07 嘉兴亚航信息技术有限公司 LNG dual-fuel power ship gas supply system
CN114754289A (en) * 2022-05-07 2022-07-15 威海中远海运重工科技有限公司 LNG ship low-pressure gas supply system and method

Similar Documents

Publication Publication Date Title
CN109185693A (en) The natural gas high-low pressure integrated gas supply system of large-scale double fuel Power Vessel
CN104265512B (en) High-pressure/low-pressure gas supply system of ship power plant
CN203162531U (en) High-pressure gas supply system of marine power plant
US6907735B2 (en) Hydrogen fueled electrical generator system and method thereof
WO2021008620A1 (en) Gas supply system employing two fuels for use in ultra-large container ship, and ultra-large container ship
CN104704229A (en) Supplying gaseous fuel from a liquid state to an engine
CN210083520U (en) Dual-fuel transport ship with high safety performance
CN204060975U (en) A kind of high voltage/low voltage fuel gas supply system of Ship Power Equipment
CN202252834U (en) Wharf boat LNG (liquefied natural gas) filling station
CN114458444A (en) Ship liquid ammonia supply system and ammonia fuel power ship
CN104534277A (en) Gas supply system and method for outputting high-pressure gas and low-pressure gas simultaneously
CN113047996A (en) Methanol fuel dual-fuel supply system
CN104334449B (en) The method changing steamturbine dynamic liquefaction natural gas carrier vessel
CN104696186A (en) Pressure boosting unit provided with LNG (liquefied natural gas) pumps connected in parallel
JP2015127510A (en) Vessel fuel supply system
CN102425725B (en) System and method for reclaiming boil off gas (BOG) in liquefied natural gas (LNG) storage tank
CN201425158Y (en) Vehicle liquefied natural gas self-pressurizing system
CN208486947U (en) A kind of combustion steaming united fuel system of bavin
CN206346844U (en) LNG composite air supplies system peculiar to vessel
KR101307100B1 (en) Multiplex power generating system improving efficiency of the marine engine
CN206346845U (en) BOG is used as dual fuel engine peculiar to vessel and supplements fuel air supply system
Cwilewicz et al. Prognosis of marine propulsion plants development in view of new requirements concerning marine fuels
CN202946925U (en) Vehicular skid-mounted liquefied compressed natural gas (LCNG) recovery system
CN104456066A (en) Economic type fuel supply device applicable to small-size LNG power ship
CN107914860A (en) Intelligent liquefied natural gas generating ship

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
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20190111