Common Pumping Liquids

Clean water
To bring all pump test curves to a common base, pump characteristics are based on clear water at ambient temperature (generally 15℃) with a density of 1000 kg/m³.
The most common material of construction for clean water is all cast iron construction or cast iron casing fitted with bronze internals, When pumping clean water, or water better defined as neutral with a specific gravity of 1 with no solids present, end suction pumps and horizontal split casing pumps are most commonly used. When high discharge heads are required, multistage type pumps are used.
When designers are limited for pump house space, vertical units of either mixed flow, axial or turbine type pumps are used.

Sea water as a corrosive medium
Sea water has a total salt content of about 25 g/ℓ. About 75% of the salt content is sodium chloride NaCl. The pH-value of sea water is usually between 7,5 and 8,3. In equilibrium with the atmosphere, the oxygen content at 15℃ is about 8 mg/ℓ.
Degassed sea water
In certain cases, sea water is degassed chemically or physic-ally. As a result of this, the aggressiveness declines considerably. In the case of chemical degasification, it should be noted that degassing takes time. Consequently, it is very important that the degasification operation, i.e. removal of the oxygen, is fully completed before the sea water enters the pump.
Care must be exercised in operation-aeration may occur through the inrush of air. Even though the inrushes are limited time-wise, damage to the materials may rapidly occur under certain circumstances if the presence of oxygen is not considered when the materials are selected. If inrushes of oxygen cannot be excluded during pump operation, it must generally be assumed that the sea water contains oxygen.
Brackish water
The term ‘brackish water’ infers a fresh water strongly con- contaminated with sea water. As far as the selection of material is concerned, the same directives apply for the transport of brackish water as for sea water. In addition, brackish water frequently contains ammonia and/or hydrogen sulphide. Even a low content of hydrogen sulphide, i.e. in the region of a few milligrams per litre, causes a pronounced increase in the aggressiveness.

Sea water from underground sources
Salt water from underground sources frequently has a much higher salt content than sea water, quite often it is about 30%, i.e. just under the solubility limit. Here again, common salt is the major constituent. The pH value is usually comparatively low (down to about 4), i.e. the water is acidulous. Whereas the content of oxygen is very low or even nonexistent, the H₂S content may amount of a few hundred milligrams per litre.
Such acidulous salt solutions containing H₂S are very corrosive and call for special materials.
As a consequence of the high salt content and depending on the operating conditions, one must expect a certain degree of salt precipitation. In such cases, suitable countermeasures must be taken in respect of the design, operation and the selection of material.
Corrosion in sea water
The materials employed have not only to exhibit sufficiently high resistance to uniform corrosion, but also against local corrosion particularly pitting and crevice corrosion. Such corrosion phenomena are experienced especially with selfpassivating ferro alloys (stainless steels). So-called ‘standby’ pumps, which are only operated intermittently, run the risk of standstill corrosion; flooding with fresh water prior to a shut-down period or periodic start-up is considered advantageous.
The various sea water pump components should be made from materials of the same type in order to prevent galvanic corrosion. The potential difference between the individual materials is to be as low as possible. However, if unlike materials have to be employed for design reasons, the surfaces of the less noble metal in contact with the water should be large in comparison with those of the noble metal. Figure 5 provides information on the danger of galvanic corrosion when different type materials are combined.
High velocities can lead to erosion corrosion. The consequences become increasingly serious, the more aggressive the medium, and the higher its velocity. Whereas the flow rate affects the behaviour of stainless steels and nickel alloys to only a minor degree, the position is reversed where unalloyed ferrous materials and copper alloys are involved. Figure 6 provides qualitative information on the influence of flow rates. Due consideration must be given thereby as to whether the medium contains oxygen or H₂S. Large quantities of H₂S tend to exclude the presence of oxygen; in such cases, the medium is slightly acidulous, down to a pH of 4.
Material behaviour
Table 1 makes recommendations for pump materials or their combinations. Unless otherwise stated, the following information applies for sea water without any H₂S content.
Unalloyed steel and cast iron
Unalloyed steel is unsuitable for sea water, unless it is provided with a suitable protective coating. Cast iron is only to be used for low velocities (possible for casings); in this case normal cathodic protection of the other internals should be employed.
Austenitic Ni-castings
Ni-Resist 1 and 2 are only suitable for medium velocities (up to about 20 m/s).
Galvanic Corrosion In Sea Water At 5-30℃

Post time: Mar-11-2025