Use

Secondary treatment of residential black water.

Total oxidation biological treatment plants are the right

equipment to achieve a high level of purification in wastewater

generated in restaurants, hotels, camping and houses without

sewer connections. Total oxidation biological treatment plants

can be installed directly downstream of the degreaser to allow

the drain of purified water directly into a watercourse, without the

risk of polluting the environment. An Imhoff or ST sedimentation

tank are installed downstream of the plant with a system (electric

pump or airlift) which recirculates the sludge within the FOT.

Operation

The active sludge biological process refers to a type of aerobic

treatment conducted by aeration of the wastewater in a biological

reactor in the presence of a microbial population (biomass). In

activated sludge plants, the bacterial populations, constituted

by numerous microorganisms, are produced continuously within

the reactor following the biochemical reactions of degradation of

organic carbon and nutrient utilization, resulting in the synthesis

of new cellular material. The activated sludge plants are equipped

with blowers that increase the presence of oxygen inside them

thereby increasing the capacity of the degradation of the organic

load by aerobic bacteria. In fact, these bacteria exploit the oxygen

to consume the biodegradable material, and the greater the

presence of oxygen, the greater is the ability to “consume” the

biodegradable organic material inside the tanks. Total oxidation

biological treatment plants are designed for volume not exceeding

0.25 (Cv < 0.25 BOD/m

3

) and daily organic volume not exceeding

60 g/P.E. The total oxidation biological treatment plant does

not include the inner decanter (sedimentation chamber) as

the high flow of oxygen permits the total oxidation of sludge,

but a sedimentation is necessary through Imhoff or ST tank

with appropriate system (electric pump or air lift) which will re-

circulate the sludge within the FOT.

Maintenance

For the correct management of the FOT plant and to achieve the

required purification results, please follow these guidelines:

Regularly inspect the FOT to check that there is no gross

material received accidentally to clog the pipes;

Regularly check that no anomalies have occurred to the

electrical panel if present;

Verify that the diaphragm blower works properly, that is,

movement must be observed in the volume of oxidation

coinciding with the operating time;

Every six months carry out the removal of excess sludge. Such

removal must be carried out by a specialized company;

As provided for by the Consolidated Act on Water (Legislative

Decree 152/06 as amended), and suggested by the normal

hygiene practice, periodically inspect and wash the inspection

well;

Specification Item

Totaloxidationbiologicaltreatmentplantsforthesecondarytreatment

of residential wastewater manufactured in rotational polyethylene,

in a single structure, free of joints and with reinforcement plate, and

equipped with inlet and outlet holes, a digestion tank and inspection

and sampling lids. Suitable for underground installation. The system

must be equipped with blower and micro-bubbles diffuser, according

to the plant specifications. The low-load activated sludge treatment

plant has been designed in compliance with the indications given by

experience, in particular, it has a retention time in the treatment stage

of approximately 22 hours and the indications summarised below:

RESIDENTIAL WASTEWATER

SECONDARY TREATMENT - DRAIN TO WATERCOURSES

PROJECT PARAMETERS

Water supply per P.E.

lt/d

200

Average flow (Q24) per P.E.

lt/h

8,3

Peak flow (Qp) per P.E.

lt/h

20

Specific organic load

gr BOD

5

/P.E.x d

42

Concentration of the biodegradable fraction

mg/l

240

COD/BOD

5

1,67-2,2

Total daily nitrogen load per P.E.

kg/P.E.x d

<0,012

Total surfactant concentration

mg/l

<15

Concentration of oils and fats

mg/l

<10

Retention time in the treatment stage

h

22 c.a

Air flow supplied to the process per P.E.

m

3

/h

0,45

Oxygen fed to the system per P.E.

m

3

/h

0,09

Figure 6

System composed of DG, IMHOFF, FOT models for domestic use, with drain into watercourses

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