METHOD OF SEWAGE TREATMENT

Abstract: The present invention refers to a process for wastewater treatment, wherein the amount of soluble organic matter is reduced by means of addition of nitrate. A relief of the wastewater treatment plants is obtained by the fact that the agent is added as early as possible in the pipeline net. The addition of nitrate may be controlled by measurement of the redox potential.

Description: METHOD OF SEWAGE TREATMΓMJ Field of invention The present invention relates to treatment of different kinds of wastewater, wherein the amount of dissolved organic compounds by addition of nitrate compounds is reduced as well as the fact that formation of hydrogen sulphide is prevented. Prior art Treatment of wastewater is an important and costly operation in society. Several methods are developed and at work. Municipal wastewater is characterized by the composition of mainly the following parts: - toilet water - bathing, washing and cleaning water from households - various industrial wastewaters - surface water Municipal wastewater is characterized by the following data: flow 0.3-0.5 m /person and day temperature 5-20°C Kjeldahl-N 20-50 g N/m 3 total-P 3-5 g P/m 3 BOD- refers to biological oxygen demand which is used as a measure of the content of easily degradable organic matter in the water. The figure 7 indicates that it is the oxygen demand during seven days in a sample kept in darkness at 20 C which is intended. TSS refers to total suspended solids and designates the amount of non-solved constituents in water or sludge. Chemical oxygen demand is called COD and defines the consumption of a certain oxidation agent, converted into oxygen demand, at oxidation of mainly organic materials in water under specified conditions. Kjeldahl-N defines that the content of nitrogen is determined according to Kjeldahl's method. Society of today has gradually increased its demands for treatment of wastewater. At present there are demands for >90 percent reduction of B0D-, TSS and phosphorus for municipal wastewater. Increasing demands and large-scale production advantages have led to the building of large, centrally placed, wastewater treatment plants in many municipals. This has resulted in extensive pipe line systems for transport of wastewater from the more peripheral parts of the municipals up to the wastewater treatment plant. In many cases the time of residence can be 1 to 2 days in the pipe line system. Thereby poisonous and corrosive hydrogen sulphide is formed under anaerobic conditions. In spite of the fact that many different methods for treatment of municipal wastewater have been developed, the present technique might roughly be divided into the following partial steps: - coarse cleaning through screen - sand sifter - pre-sedimeπtation - biological treatment, often active sludge SUB ST ITUTESHEET - phosphorus precipitation by chemical precipitation/flocculation. In order to increase the efficiency of the wastewater treatment plants chemical precipitation has more and more been used in connection with pre-sedi entation, so-called pre-pre- cipitation, whereby almost all particularly bonded pollutants can be separated. However, solved BOD is not separated to any larger extent. The sludge separated from presedimentation and biological treatment is often stabilized by means of digestion in a digester, whereby inter alia methane gas is formed. The gas is usually flared but in recent years it has more and more begun to be used for energy production. Description of the invention The object of the present invention is to reduce the amount of organic pollutants, especially oxygen demanding substances, in an early stage, and/or to prevent that solid pollutants are transmitted into a solution phase. This gives an overall better treatment and reduces the load of the subsequent steps, which increases the possibilities for additional connections and/or new treatment processes. The proposed process is based on the following assumptions: 1. The wastewater contains organic pollutants mainly as solids, wherein only a part of the biochemical oxygen demanding material is present in a soluble form. 2. The wastewater is given such a long time of residence before the final treatment step that added nitrate will have time to be consumed, preventing the total nitrogen amount in the effluent to be increased by the addition. 3. Great demands are called for at the treatment of wastewater, especially concerning BOD.,, TSS, N and P. At the process according to the invention the pipe line net or other residing volume are exploited for the following SUBSTITUTE SHEET purposes: 1. To reduce soluble oxygen demanding matter. 2. To prevent transformation (degradation) of solid organic matter to solved or colloidal compounds which are difficult to separate. 3. To reduce soluble organic phosphorus and nitrogen. The method can be used in larger sewer nets, in average sized or large wastewater treatment plants, in smaller waste- water treatment plants, in wastewater plants for single house¬ holds or in connection with the handling of sludge in transport vehicles as well as for industrial wastewaters with a high amount of oxygen demanding matter. The effect is achieved by addition of an active oxidation agent, viz. nitrate ions in the form of calcium or other nitra¬ tes or in the form of nitric acid, early or successively in the pipe line system, possibly in combination with measures in order to control the time of residence and the microorganism flora in the pipe line net by means of recirculation, damping, extra volume, graft, etc. A suitable way of adding the nitrate is in the form of a solution. The nitrate may also be combined with other oxidation agents, e.g. trivalent iron, air or oxygen or a combination of these, to mention some examples. By addition of oxidation agents the microbial activity in the pipe line net is stimulated and a certain amount of the oxygen-consuming sub¬ stance is oxidized or transmitted to sludge particles. The result will be a reduction of mainly soluble BOD. In addition, a reduction of soluble organic phosphorus by means of a trans¬ formation to PO.-P takes place in the pipe line net or in other retentive volumes. This entails that a more effective phosporus precipitation is obtained in the chemical precipi- tation step of the wasterwater treatment plant. The normal transformation from soluble organic nitrogen to ammonium nitrogen is also increased. S UB STITUTESHEET By means of this process a great part of the activity, which otherwise takes place in the wastewater treatment plant is transferred to the pipe line net. The process increases the capacity and gives more stable operation conditions in the wastewater treatment plant by the fact that the aerobic biological activity is accelerated. The wastewater treatment plant is thereby given an essential relief with, as well as without pre-precipitation. The result is a very good total pollution reduction. In this way the need of energy for aeration also may be reduced. By means of the choice of oxidation agent and/or precipitation chemicals, the addition of chemicals, in the pre-precipitation or totally, can be reduced. The invention gives opportunities of new combinations of known technique and of new concepts for wastewater treatment. It also increases the possibilites of additional treatment, e.g. nitrogen reduction. The amount of nitrate which is required for a good result is important and the addition of nitrate can be controlled according to the residence time in the net, by analyzing TOC (total organic carbon), COD or redox potential. SUBSTITUTESHEET

Claims: CLAIMS 1. Process for wastewater treatment comprising a reduction of the amount of soluble organic matter by addition of nitrate before the final treatment, e.g. chemical prepipitacion, biological cleaning, etc. c h a r a c t e ri z e d in that nitrate is added in an early stage and that the amount of added nitrate is controlled by the amount of oxygen demanding matter before the final treatment. 2. Process according to claim 1, c h a r a c t e r i z e d in that the nitrate is used alone or in combination with other oxidation agents, e.g. oxygen, air or trivalent iron. 3. Process according to claim 1, c h a r a c t e r i z e d in that _the residence time in the pipe line net is extended by means of repumpiπg or recirculation in the pipe line net, by damping or by residence giving volume or device.

Inventors: HAEGERSTEDT LARS-ERIK, HAEGERSTEDT, LARS-ERIK
Applicants: SUPRA AB, SUPRA AKTIEBOLAG
Application year: 1989
Main classification: C02F1
IPC codes: C02F1, C02F3