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Thursday, September 18, 2025

BWTS OZONE TYPE BASICS

MARINESHELF publishes articles contributed by seafarers and other marine related sites solely for the benefit of seafarers .All copyright materials are owned by its respective authors or publishers.

Ozone is a natural gas which forms in the atmosphere when an oxygen atom (O) joins with an oxygen molecule (O2) to form ozone (O3). This reaction requires the input of energy (such as a lightning strike), to join the oxygen atom with the oxygen molecule. As soon as the energy source is removed, the ozone immediately decomposes. Ozone is a colorless gas but has a very pungent odor. Although ozone has an extremely short life-span, it is one of the most powerful oxidizing agents produced and effectively neutralizing endo-toxins, viruses, bacteria, fungi and organic material extremely rapidly. Usually a ship-board Ozone generator takes ambient air and strips away the nitrogen, concentrating the oxygen content – which is then passed through a high voltage or high frequency electrical field to produce ozone. The ozone is then injected into the incoming ballast water to oxidize and neutralize any harmful aquatic species. A percentage of the aquatic species, especially any bacteria and viruses in the ballast water, are killed by direct contact with the ozone. The remainder are killed or neutralized when the ozone reacts with other chemicals that occur naturally in seawater, to form hypobromous acid, a highly effective disinfectant in its own right. Both ozone and hypobromous acid disintegrate extremely rapidly – ensuring that there is no damage to the receiving waters into which the treated ballast water is discharged. Air contains 21% oxygen, 78% nitrogen, 0.9% argon, and 0.1% other gases.

These system usually consists of an Air compressor that produces between 5 and 8 bar of compressed air by inhaling the air of the atmosphere and provides compressed air to oxygen generator through air receiver; as raw material for oxygen generator.

 

In the NK -O3  type Ozone system the  Oxygen generators separate oxygen from compressed air through a unique Pressure Swing Adsorption (PSA) process. The PSA process uses two vessels filled with molecular sieve (a synthetic zeolite)

As compressed feed air flows through one of the vessels, the molecular sieve adsorbs nitrogen. The remaining oxygen passes through the vessel and exits as the product gas. Before the absorber becomes saturated with nitrogen, the feed air is diverted to the second vessel. At that point, the sieve in the first vessel regenerates by desorbing the nitrogen through depressurization and purging it with oxygen from the second vessel. This process is then repeated in the second vessel to complete a cycle that allows the oxygen generator to deliver a constant flow of product oxygen at 90% minimum purity. Under normal operating conditions, the molecular sieve is completely regenerative and will last indefinitely.

Air and oxygen receiver provide stabilized flow and pressure to the oxygen and ozone generator by reducing the pulsation respectively.

Air receiver stores compressed air for peak demand in excess of compressor flow rate. Air receiver increases the cooling of the compressed air and collects possible residual condensate and oil droplets. The pressure variations in the air net will be equalized and short cycle loading and unloading of the compressor minimized. Ozone is generated by converting part of the oxygen gas molecules O2 within a gap formed between two electrodes. When applying an alternating high voltage to the high voltage electrode, micro-discharges will take place in the discharge gap which will dissociate the oxygen molecules. Some of the freed oxygen atoms O will recombine with the remaining oxygen molecules O2 to form ozone O3. This principle is usually called "Silent Electrical Discharge".

O + O2 = O3 

The ozone concentration of the gas at the outlet of the generator is expressed by the ratio of the ozone mass produced divided by the total outlet gas mass (% by weight) or the mass of ozone produced per volume of outlet gas (g/Nm3 ).

The ozone generation modules are cooled with water to efficiently remove all the heat generated by the generated by the process. Ozone generation is very sensible to the cooling water temperature and the gas quality. The lower the temperature, the higher the ozone efficiency will be.

An Ozone destructor is used to converts any unused ozone back to oxygen before release to the atmosphere. The ozone destructor is used to run the ozone system without injecting the ozone in the ballast water. It will help to evaluate the good operation of the ozone system.

Due to the hazardous and corrosive nature of ozone even in low concentrations, no ozone containing gas should be released into the atmosphere. The residual ozone concentration according to the safety requirements of lower than 0.2 ppmv will be observed. The unit comprises welded stainless steel housing and the catalyst. The destructor works according to the principle of catalytic ozone destroying. The gas flow to be treated will be passed through the catalyst. The residual ozone in the off-gas will be converted into oxygen on the surface of the composition metal catalyst. The off-gas flow has to be vented into open air. During this process, heat of reaction is released.

                                   

                                                      A schematic dwg of an NK system

Ozone injector is very important equipment for ballast water treatment system using ozone as disinfection material. To increase disinfection effect and reduce toxic by-products, ozone should be introduced very quickly and uniformly to ballast water.

The Neutralizer is designed to remove Total Residual Oxidants (TRO) from ships’ ballast water that has been treated by the Ozone System. The Neutralizer makes the TRO concentration below 0.4mg/L by dosing neutralizer automatically, prior to discharge of the treated ballast water. Thiosulfate is usually  used in the TRO neutralizer

 Ambient ozone monitors can be tripped by the ozone leak in the ozone system. When an ozone alarm has been given the ozone production must be interrupted. All personnel must be evacuated from the contaminated area. The room containing ozone should only be entered when wearing a suitable breathing apparatus.

The TRO analyzer uses colorimetric DPD chemistry or an electrical TRO sensor to continuously monitor water for TRO.

Sunday, September 14, 2025

BWTS ELECTROLYSIS TYPE BASICS

MARINESHELF publishes articles contributed by seafarers and other marine related sites solely for the benefit of seafarers .All copyright materials are owned by its respective authors or publishers.

At ballasting the ballast water treatment process performs two main unit operations: mechanical separation (filtering) and disinfection (electrolysis based chlorination). In the first step, the filters (50 μm filter fineness) remove particles, sediments and organisms of the larger size class. This allows the following disinfection step to minimize the use of NaOCl, a chlorine compound. In the second step, the sodium hypochlorite solution generated from the electrolysis unit is injected into the filtered influent ballast water to effectively disinfect organisms of the smaller size class and bacteria remaining in the filtrate. At de-ballasting, neutralization unit decreases the total residual oxidants (TRO) concentration if required before the ballast water discharge.

A Back-flushing Filter is installed on ballast pump discharge line and it will filter

organisms and particle materials over than 50 micrometers. There is back-flushing line on Back-flushing Filter for cleaning itself. Usually Back-flushing Filter is combined with one(1) set of Back-flushing Pump which supplies clean seawater for cleaning. A Back-flushing Valve is installed on Back-flushing Filter discharge line and it makes more pressure on Back flushing Filter to help back-flushing operation. Back-flushing Pump and  Back flushing Valve are installed on back-flushing line for pumping out back-flushing water overboard.


                                             

 After this filtering process, second disinfection process of generating and injecting biocide(Sodium hypochlorite, NaOCl) are as follows. Electrolysis unit electrolyzes seawater that is coming from the separate branch line from main ballast line. Only 0.5% of total ballast water flow is used for producing disinfectant solution. Booster Pump is installed on this line to pumping the clean seawater to Electrolysis Unit. Seawater should be met that temperature over than 5and salinity over than 10 PSU. If seawater does not meet these conditions, A Heat Exchanger will be used.

High salinity seawater shall be loaded in the separated seawater tank (sometimes also called technical sea water tank ) in advance and it will be used when the vessel goes to the brackish water zone. Temperature sensor and salinity sensor give alarm to the crew. And after, seawater flows into the Electrolyzer , Seawater is electrolyzed in the Electrode. The concentration of generating biocide in Electrode is decided by current control of Rectifier. When the seawater electrolyzed, hydrogen gas, oxygen gas and chlorine gas are generated as byproduct. These gases are

separated in the hydrocyclone and vented out safely after diluted by blower. There is gas monitoring system on vent line. When the biocide solution injected to main ballast line, injection rate is controlled by Flowmeter and Flow Control Valve.

 After injecting to the main ballast line, final concentration of TRO is checked by TRO

sensor and the data transmitted to MCP for current control.

Flowmeters  on main ballast line checks flow rate of ballast water.

After Peak Tank is located in the aft of the vessel and it is separated with main ballast system. So, BWMS system is designed to treat the seawater separately of those two ballast system

Bypass mode is operated only in emergency case. In this mode, seawater flows into the ballast tank directly without any treatment. This operation shall be recorded in the system.

For deballasting operation TRO CONCENTRATION > 0.1ppm  always and zero for USCG mode.For Ballasting operation TRO value has a range and is not than 7ppm.

Saturday, September 13, 2025

EGCS BASICS

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Seawater is the main absorbing medium used in the exhaust gas cleaning process. Seawater is alkaline and thus offers a buffer and neutralization capacity. Seawater also contain large amounts of dissolved sulphates. The absorbed SO2 will only marginally increase the seawater content of sulphates. Commercial available NaOH solution (50%) is injected in both cleaning stages to boost the seawater alkalinity and thus increase the neutralization capacity and the absorption efficiency in the EGCS. This boost will also compensate for the fluctuating alkalinity content in the ambient seawater, and will reduce the amount of seawater used and raise the pH of the washwater.



Through efficient interaction between the highly alkaline seawater and the exhaust gas stream, SO2 and also particulate matter (PM) is dissolved in, or captured by, the liquid.

When dissolved in the liquid, SO2 originating from the burnt fuel oil will make the liquid acidic before the alkalinity in the water convert the sulphur to harmless sulphites/sulphates. Such sulphites/sulphates may be discharged to sea without further treatment.



SO2 is dissolved in seawater (reaction a), it reacts with water and forms an acid, H+ ions are produced (i.e pH decreases). Bicarbonate and carbonate in the seawater reacts with the released H+ , thus neutralizing part of the acidic effect from the absorbed SO2. The sulphite will react with the oxygen in the seawater and form sulphate (reaction c). Adding caustic soda (NaOH) to the seawater will increase the neutralizing capacity, last two reactions.



The washwater is monitored by measuring pH, PAH and turbidity. If the washwater exceeds given limits for turbidity and PAH, then a part of the washwater ("1st stage injection drain") may be cleaned through the Water treatment filter before being discharged to sea. Residue from the filter will be contained on board before being discharged to shore.

The system may operate in the following modes:

Open loop mode

Closed loop mode

Open loop reduced load mode

Closed loop reduced load mode

 

OPEN LOOP

Seawater is used as cleaning liquid and pass through the system once before being

monitored and then discharged to sea.

The seawater alkalinity is boosted with NaOH to increase the SOx absorption

A part of the washwater ("1st stage injection drain") is collected in the gas inlet section of

the scrubber, and this stream may be cleaned in the Water treatment filter before

discharge.

 

CLOSED LOOP (Alternative system)

Washwater is used as cleaning liquid and is recirculated through the system via the System

tank and Recirculation pump.

The washwater alkalinity is boosted with NaOH to increase the SOx absorption.

To avoid saturation, a bleed stream is drained from the Decanter tank to the Holding tank and a balancing amount of makeup water (seawater) is added to the System tank.

The recirculated washwater is cooled before being re-injected to the EGCU.

A part of the washwater ("1st stage injection drain") is collected in the gas inlet section of the scrubber, and this stream is cleaned in the Water treatment filter before recirculation.

 Provision of two basic Schemes for compliance to be used for EGCS approval, Scheme A or Scheme B, as the choice of the equipment manufacturer.

The two EGCS schemes apply the following concepts:

 Scheme A - based on initial emission performance unit certification together with a continuous check of operating parameters and daily exhaust emission monitoring

• Scheme B - based on continuous exhaust emission monitoring together with a daily check of operating Parameters

 REQUIRED EGC SYSTEM DOCUMENTATION

 On board Documentation

SECP Sox emission compliance Plan

ETM-B EGCS technical Manual Scheme – B (ETM – B)

OMM Onboard Monitoring Manual

EGC Record Book or Electronic Logging system


The system consists of 2 water monitors:

No. 1 is installed close to the scrubbing water pumps measuring the (inlet) scrubbing water parameters pH and Turbidity, the pH value is used for monitoring purpose and to give alarm is it is too low, the Turbidity value is used to deduct it from the outlet value as the outlet limitations are above the inlet.

No. 2 is installed on the outlet of the system close to the over boards, measuring the

Wash water parameters pH, Turbidity and PAH (Poly Cyclic Aromatic Hydrocarbons)

-pH limits are different for each system and is specified in the ETM-B for the specific vessel.

-Turbidity limits are 25NTU with an exceedance allowance of 20% for every 12-hour period.

-The PAH limits are also different for each system and is stated in the ETM-B for the specific vessel. This parameter has also has an exceedance allowance of 100% of the limit for every 12-hour period.

 

 


Friday, September 12, 2025

WILL SHIPFINEX BE A GAME CHANGER IN SHIPPING

MARINESHELF publishes articles contributed by seafarers and other marine related sites solely for the benefit of seafarers .All copyright materials are owned by its respective authors or publishers.

                       
                    

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