Wastewater disinfection with a combination of biocides

Abstract: Wastewater is effectively disinfected while reducing both chlorine consumption and more particularly the levels of residual chlorine discharged from the wastewater treatment plant. The wastewater is first contacted with a sufficient amount of chlorine to satisfy the chlorine demand and to obtain as low a residual level of chlorine as possible. After the chlorine demand has been satisfied, the wastewater is disinfected with an effective amount of 2,2-dibromo-3-nitrilopropionmaide.

Description: The present invention is directed to the disinfection of the effluent from wastewater treatment plants with a biocidal combination of an α-halogenated amide and chlorine. The term "disinfection", as applied to municipal wastewater, refers to a reduction in the population of pathogenic organisms, generally bacteria species. Since several different bacteria species are known to be present in wastewater, an indicator organism for which specific monitoring methods are available is used to monitor disinfection, such as the bacterium Escherichia colt which is known to exist in human fecal matter. The effluent from a wastewater treatment plant (WWTP) is considered to be "disinfected" if the number of indicator organisms per volume of effluent falls at or below a preset health guideline, typically established by governmental agencies. A typical health guideline may mandate daily testing for fecal coliform bacteria and may stipulate limits such as "less than 200 per 100 mL effluent" for the geometric mean of 30 days of tests and such as "less than 400 per 100 mL effluent" for the geometric mean of 7 days of such tests. Since the early part of the twentieth century chlorine has been commonly used to disinfect wastewater. Although several chlorine-releasing chemicals may be used to accomplish this, a more typical method is for chlorine gas to be added to the wastewater directly. This is usually one of the last or the last treatment in a municipal WWTP. Sufficient chlorine must be added to satisfy the "chlorine demand" of the water being treated. When chlorine is added to wastewater at low concentrations, a fast reaction occurs with various organic species, including naturally occurring chemicals such as fulvic and humic acids. The initial amount of chlorine which reacts in this fashion is said to be satisfying the chlorine demand. The demand of different waters will vary depending on the amounts of organic species present. Once the demand is satisfied, addition of more chlorine will result in a chlorine residual which is detectable by various analytical means. It is the residual chlorine which is available as an oxidizing biocide to disinfect the water. The level of chlorine residual required to disinfect WWTP effluent varies from one plant to another and within the same plant due to variations in the specific wastewater being treated. Some plants may be able to disinfect with a chlorine residual of 0.1 parts per million (ppm) whereas others may require greater than 2.0 ppm. Typical levels of chlorine residual required for disinfection would be in the range from 0.3 to 1.0 ppm. Until recently, chlorine residual limits have been relatively high and plants have generally not had problems maintaining disinfection. However, health and safety considerations now suggest that chlorine residuals be controlled and limited. Specific concerns about chlorine stem from fish toxicity, fish avoidance of the zone in which chlorine is discharged, formation of chloramines (reaction products of chlorine and ammonia which are also toxic to fish and which persist longer than chlorine), and formation of halogenated methanes as a result of chlorine addition. As a result of these concerns, it is now proposed by many governmental health and safety agencies that the previously accepted chlorine residual level of 1.0 ppm be significantly reduced, preferably to 0.036 ppm. However, most, if not all, WWTP's would not be able to meet the requirements for disinfection with chlorine residuals below 0.036. In an attempt to reduce the level of chlorine in the effluent, some WWTP's are adding sulfur dioxide feed systems. Sulfur dioxide, when added to the effluent, will react with the residual chlorine rapidly and cause the measurable residual to diminish to non-detectable. There are numerous disadvantages to this technique, including the capital cost of installing the feed system, the on-going chemical cost, the operating and maintenance expense, the possible effects on the chemistry of the effluent, the reporting requirements for leaks, and the relative lack of data on the environmental impact of sulfur dioxide. Ultraviolet disinfection and ozonation as a means of disinfection have both been proposed. While both are theoretically possible, neither has proven to be reliable in WWTP's. Moreover, the cost of either technique is very high, involving both high capital expenses and high operating and maintenance costs. Polishing ponds have also been proposed as a means to meet new requirements. These are merely holding basins in which wastewater effluent is exposed to the environment for some time period after disinfection and the residual chlorine is allowed to dissipate naturally. Use of this technology requires considerable space, which could necessitate the purchase of land. In addition, installation of the polishing pond for even a small WWTP is costly. This method will also result in the re-growth of bacteria prior to discharge of the effluent. Thus, what is needed is a method that would allow WWTP's to lower the addition of chlorine to a point where chlorine residuals would be acceptable to meet health, safety and environmental concerns while simultaneously maintaining required levels of disinfection. The present invention is directed to a method for disinfecting wastewater which comprises contacting the wastewater to be disinfected with an effective amount of chlorine to provide a residual level of 0.005 to 0.05 mg/L and contacting the chlorine treated wastewater with an effective amount of 2,2-dibromo-3-nitrilopropionamide (DBNPA) to disinfect the wastewater. Preferably, an effective amount of DBNPA is 0.07 to 0.5 mg/L. DBNPA is an effective biocide which rapidly degrades to carbon dioxide, bromide ion and ammonia. Because of the rapid degradation of DBNPA, it is a more environmentally acceptable material than chlorine. The use of chlorine and DBNPA for wastewater disinfection allows for a substantial reduction in chlorine usage with a concomitant reduction in residual chlorine levels while maintaining prescribed levels of disinfection. This is accomplished with a minimum of capital and operating expenses. Figure 1 is a 3-dimensional graph illustrating the disinfection of effluent from a WWTP by combinations of DBNPA and chlorine. Figure 2 is a graph illustrating the monthly data from the West Bay County, Michigan wastewater treatment plant over a nine-month period with respect to fecal coliform counts, biological oxygen demand (BOD) and suspended solids while using 0.1 mg/L of DBNPA with residual chlorine. Figure 3 is a graph depicting average daily chlorine consumption at the West Bay County, Michigan wastewater treatment plant both before and after using DBNPA. In the practice of the present invention, chlorine is added to the wastewater at the entrance of a chamber that will provide contact time as illustrated in Figure 1. The level of chlorine is typically adjusted to obtain a residual level at the end of the contact time as low as possible, that is, as low as can be routinely measured. The residual must be greater than zero in order to satisfy the "chlorine demand." Continuous on-line monitoring of chlorine residual is preferred over periodic sampling. Best results are obtained when the chlorine is rapidly distributed in the wastewater. Adequate mixing can be provided by conventional equipment such as pumps. The DBNPA is added as soon as possible and at a point after the chlorine demand has been satisfied. Again, rapid mixing is preferred. A mixing pump, for example, can be placed adjacent to the DBNPA feed point. If chlorine demand is not satisfied prior to addition of DBNPA, then breakdown of DBNPA will be hastened and additional product will be required to accomplish disinfection. The mechanism for feeding chlorine into a wastewater treatment system is well-known in the industry. Feed of the DBNPA can be accomplished via a suitable pump, for example, a chemical metering pump and tubing constructed of materials inert to DBNPA. In WWTPs where the flow is not constant, it is preferred that the feed rates of both chlorine and DBNPA be flow-proportioned. Chlorine flow should be monitored and adjusted as necessary to maintain a barely detectable residual. The method of the present invention is effective under most climatic and operational conditions typically encountered. For example, the present invention is effective at temperatures ranging from -20°F (-28.9°C) to 105°F (40.5°C) and at all pH levels usually experienced in WWTPs. Effective concentrations of DBNPA range from 0.07 to 0.5 mg/L of effluent when used in conjunction with residual chlorine. Preferably, from 0.10 to 0.20 mg/L of DBNPA are employed with residual levels of chlorine ranging from 0.05 to 0.005 mg/L. High levels of biological oxygen demand (BOD) or suspended solids may require higher levels of DBNPA. The following examples illustrate the present invention but are not to be construed as limiting the same. Example 1 Wastewater disinfection with mixtures of DBNPA and chlorine The West Bay County, Michigan Plant is a 4 million gallon per day (mgd) (0.175 m³/s) facility serving the communities surrounding Bay City. The influent is predominantly domestic waste, with a potato chip manufacturer being the largest year-around source of industrial waste. During the winter months, a beet sugar mill provides most of the industrial waste. The plant uses primary and secondary treatment followed by disinfection. Disinfection had previously been done with chlorine alone and required a residual of 0.6 mg/L to control fecal coliforms adequately. The chlorine contact chamber provides about 20 minutes of contact time, although channeling allows some breakthrough in 10 minutes. Disinfection is required all year due to proximity of the discharge to the drinking water source for the County. The disinfection criteria are a geometric mean fecal coliform count of less than 200 per 100 mL over a 30-day period and less than 400 per 100 mL over a 7-day period. Fecal coliform counts were determined by conventional procedures. To determine the effectiveness of the DBNPA plus chlorine combination, initial rangefinding studies were conducted on one side of the two-sided contact chamber. The total residual chlorine (as determined by amperometric titration of grab samples) was lowered over a four hour period by reducing the feed rate. A tote containing 300 gallons (1.14 m³) of 20 percent DBNPA was placed adjacent to the contact chamber. Feed was accomplished by placing an adjustable rate chemical metering pump connected by flexible tubing to the tote. PVC tubing was used to connect a line from the pump exit to a point in the contact chamber immediately after the chlorine diffusers. To ensure rapid mixing, a one-half horsepower submersible pump was suspended in the chamber adjacent to the exit of the DBNPA feed. The pump was calibrated to deliver 0.2 mg/L DBNPA at the nominal flow of 2 mgd (0.088 m³/s) through this side of the contact chamber. Each week the feed rate was lowered by approximately 10 percent until the delivery was 0.1 mg/L. Due to variations in the actual flow through the plant the DBNPA feed varied from 0.07 mg/L to 0.27 mg/L throughout the test period. The chlorine residual varied similarly and during this study was adjusted manually to maintain a residual as low as possible but above zero. At least twice daily grab samples were taken at the end of the chamber for determination of total residual chlorine and fecal coliform counts. About 1 month into the study, all of the plant effluent was directed to the side of the contact chamber using DBNPA and chlorine, effectively doubling the flow and cutting the contact time in half. In general, this resulted in an overall improvement in disinfection. This most likely was due to increased initial mixing of the chlorinated effluent with DBNPA. In addition, during the first two months a liquid chromatograph was set up and used to monitor for DBNPA in the effluent. Samples were taken either 2 or 4 times daily (at all times of the day and night). The detection limit of the method varied from 0.1 to about 0.2 mg/L depending on effluent quality. At no time during the study was DBNPA detectable in the effluent. Data was collected for 5 months at DBNPA concentrations ranging from 0.07 to 2.7 mg/L. It was concluded that under routine operating conditions, 0.10 mg/L was sufficient to achieve disinfection when using chlorine at a residual of 0.036 mg/L. Table I lists the combinations of DBNPA and chlorine which were required. Exceptions were noted during the study, but they were generally able to be traced to a particular cause (for example, rapid unexpected change in influent BOD, faulty chlorine feed, etc.) DBNPA/CHLORINE COMBINATIONS WHICH PROVIDED GOOD DISINFECTION mg/L DBNPA mg/L Chlorine Residual 0.07-0.09 0.06-0.10 0.10-0.11 0.02-0.05 0.12-0.15 0.01-0.02 0.16-0.20 0.005-0.01 Figure 2 is a 3-dimensional graphic presentation of the data collected during the 5 month test period. The graph illustrates effluent disinfection in terms of fecal coliform counts per 100 mL of effluent provided by mixtures of DBNPA and chlorine at various concentrations. Fecal coliform counts below 200 counts per 100 mL are considered effective levels of disinfection. Representative examples of the raw data used to compile Figure 2 are presented in Table II. After the range-finding study, the facility began continuous application of 0.10 mg/L DBNPA. Feed rates of both DBNPA and chlorine were flow-controlled by coupling to a 4 to 20 milliamp signal generated at the Parshall Flume. A Parshall Flume is a flow-measuring apparatus consisting essentially of a trough through which the water flows, having a geometric shape which results in the depth of the water being proportional to the water flowing through it. The 300 gallon (1.14 m³) tote of formulated DBNPA was placed permanently next to the contact chamber and the pump permanently mounted on the chamber sidewall. The only deviation of the DBNPA feed level occurred during the peak of the annual sugar campaign, at which time the concentration of DBNPA was raised to 0.11 to 0.12 mg/L. A summary of the monthly data submitted by the plant for coliform counts, BOD, and suspended solids is summarized in Table III and shown in Figure 3. During this period the WWTP was disinfecting continuously with 0.1 mg/L DBNPA and low chlorine. Only the December 1987 point does not meet the disinfection criteria of a less than 200 coliform count per 100 mL. In that case the non-compliance was the result of upsets due to the beginning of the sugar campaign. With the exception of December disinfection has been acceptable. This is true in spite of normal upsets in plant operation (for example, clarifier cleaning, raw sewage pumps running, etc.). It must be noted that in spite of flow-proportioning chlorine the residual on several occasions would exceed the targeted maximum of 0.036 mg/L. The data showed, however, that the coliform counts were essentially the same if times of higher results were excluded. Chlorine usage at this WWTP has decreased dramatically since the DBNPA plus chlorine combination has been implemented. Figure 4 shows average daily chlorine consumption on a monthly basis. In the months prior to using DBNPA, average chlorine feed per day was 84 kg (185 pounds). Since starting to add DBNPA continuously at 0.1 mg/L, average chlorine feed per day has been less than 30 kg (65 pounds).

Claims: A process for disinfecting wastewater comrpising: (a) contacting the wastewater with chlorine to provide a residual level of 0.005 to 0.05 mg/L; and (b)contacting the chlorine-treated wastewater with an effective amount of 2,2-dibromo-3-nitrilopropionamide to disinfect the wastewater. The process of Claim 1 wherein the chlorine-treated wastewater is treated with the 2,2-dibromo-3-nitrilopropionamide at a point as soon as possible after the chlorine residual level has been satisfied. The process of Claim 1 wherein the effective amount of 2,2-dibromo-3-nitrilo-propionamide range is 0.07 to 0.5 mg/L. The process of Claim 1 or 3 wherein the feed rates of both chlorine and 2,2-dibromo-3-nitrilopro-pionamide are proportioned to a flow rate of the wastewater.

Inventors: KARBOWSKI ROBERT J, KARBOWSKI, ROBERT J.
Applicants: DOW CHEMICAL CO, THE DOW CHEMICAL COMPANY (A DELAWARE CORPORATION)
Application year: 1990
Main classification: C02F1
IPC codes: C02F1