Gas operations

ALONGSIDE 7 put at disposal operations for N2 and Gases under DNV-GL Certification

Nitrogen (N2)

Operatives are carried out by 2 x ISO 20´containers (L-6058 x W-2438 x H-2591mm) as mobile evaporator plant, 1 x Dry container with 4 atmospheric evorators and 1 x Cryotank which volume is able for transporting around 15000 Kg of Liquid Nitrogen at 10 Bar pressure (12.500 Nm3) to supply from 200 to 2000qm./hr. at a Tº from 5 to 40degC. of Nitrogen Gas controlled safely by 2 Fluidmeters in ranges from 100/1000 to 300/3000 Nm3/hr.

Composition: N2 > 99.995%, H2O + O2 < 10 ppm (dew point < - 60.5ºC).

Hose Connections: 4´´ASA 150, 4´´ASA 300, 3´´ASA 150, 2´´ASA 150

Attending N2 Liquid at berth by tanker truck and by Criotank at anchorage without limit of volume to be supplied and refillig tanks in 3 hours

Available N2 Gas for Cold test by mobile plant which serve up to 6000mq/hr. (-180de.C)

Gas carrier cargo handling

Typical operation cycle of most refrigerated type liquefied gas carriers includes drying, inerting, cooling down, preparation work prior to loading, loding, laden voyage, unloading, ballast voyage, stripping, warming up and gas freeing.

  • Drying – In order to prevent ice formation during cooling and to maintain the quality of products, moisture in all cargo tanks and associated piping is to be eliminated. Drying is achieved by introducing dry air into areas to be dried.
  • Inerting – Inerting is done by supplying an inert gas to cargo tanks and associated piping in order to produce non-explosive atmosphere in these areas. Two types of inert gas are commonly used: gas produced with an inert gas generator and nitrogen gas.
  • Cooling down – In order to avoid any damage to cargo tanks and piping due to thermal shock as well as to reduce the generation of boil-off gases (BOG) during loading operations, cargo tanks and piping are gradually cooled down. This procedure often consists of introducing low temperature argo vapour into the cargo tanks and piping or of spraying the tanks with liquefied cargo.
  • Loading – Cargoes are loaded into cargo tanks through cargo liquid lines by means of shore side pumps. Cargo vapour present in tanks is returned to the shore terminal via cargo vapour lines using compressors on board. Since the vapour is not vented at any time during this operation, this process is often referred to as a closed cycle one.
  • Laden voyage – Except for pressure type gas carriers, cargo Tº and pressure control is mainly carried out at sea. Boil-off gases produced at sea are sent to reliquefaction plant and returned to the cargo tanks after being re-liquefied. In the case of LNG carriers, BOG may either be reliquefied or sent to the main engines as fuel for propulsion.
  • Unloading – Cargoes are discharged using cargo pumps on board and gases are supplied from the shore side. This operation is carried out in a closed cycle. A portion of the cargo is retained in one of the cargo tanks in order to carry out cooling down operation during ballast voyage.
  • Stripping – All cargo in the tanks is completely discharged as much as possible before any warming up and gas-freeing operations are undertaken.
  • Warming up – It consists of raising the temperature of cargo tanks and their piping in order to carry out gas-freeing operation. During warming up all remaining cargo is vaporized and heated by a cargo vaporizer and heater installed onboard. The heated gas then circulates through tanks and piping to raise the temperature of the entire system.

Gas Operations / Gassing up attended by truck at berth for:

  • Propane
  • Isopropane
  • Butane
  • Ammonia

Test & inspections

ALONGSIDE 7 offer tests and inspection of LPG/LNG products for refineries, pipelines, marine and shore tank cargo storage putting at disposal
services for analytical testing, trace analysis, loss and quality control during production, storage and cargo custody transfer.

Gases analyzed include Hydrocarbons (C1 to C6+) such as Methane, Ethane, Propane, Iso-Butane, N-Butane, Iso-Pentane, N-Pentane, and Hexane.

Natural gas trace impurities include Hydrogen, Nitrogen, Carbon Monoxide, Carbon dioxide, Oxygen, Mercury, Water, and other components.

LPG/LNG Tests offered for:

  • Composition of gases
  • Non-condensableGases
  • Volatility
  • Sulfur, Sulfur Speciation
  • Ammonia, Arsine, Carbonyl, Chloride, Fluoride Volatility, Vapor Pressure
  • Inhibitor Content

Standards & Specifications:

  • ASTM D 1835
  • GPA 2140
  • GOST 20448
  • ISO 6974
  • UOP 539