Rochester Institute of Technology |
Industrial Wastewater Management
Metal Finishing
Ian Madison and Jacqueline Jordan
Industry Description
Industry Profile
The SIC code for metal finishing is 3471. There are many industries that use metal finishing in the process of creating their product. Metal finishing is an industry that has many divisions. The six main operations covered by metal finishing regulations are: electroplating, electroless plating, anodizing, coating (chromating, phosphating and coloring), chemical etching and milling, and printed circuit board manufacture. All of these processes create forms of pollution. There are reportedly 267 metal finishing shops in New York State (Sharon E. Rehder, 2000). Most of these shops in NYS are small businesses; almost half have less than 10 employees. Rehder reasons that most of the waste coming from metal finishing in NYS come from small businesses, possibly far more than reported; this is in contrast to most other industrial sectors which have a few large, well-known sources.
Water pollution is discussed in this paper. Many chemicals are used in the processes used to finish metal, whether it is plating, polishing, anodizing or coloring. One of the most disturbing reports regarding the businesses in NYS and the toxic chemicals they release is the Toxics Release Inventory (TRI). According to Rehder, only 29 of the 267 known metal finishers in the state have filed a TRI, and the amount reported to have been released is “315,156 pounds of hazardous substances to the environment”. There were no reports filed by the other 238 metal finishers, possibly due to being small enough of a business to not be required to report. However, collectively, the amount of toxic chemicals being released is significant.
Typical Processes and Products
There is a large variety of businesses that fall into the category of metal finishers. The products are diverse, widespread and used by everyone in some capacity or another. All the chrome on your vehicle starts out as either a dull metal or plastic piece. It gets coated with chromium to produce that shiny look that everyone is accustomed to seeing on their car or truck. Many other parts on autos have finished surfaces; the automotive industry is listed as the highest metal finishing industry, at 40% according to the Illinois Sustainable Technology Center. There are many types of finishing processes used: electroplating, electroless plating and immersion plating, chemical and electrochemical conversion, cladding, case hardening, dip/galvanized, electropolishing, vapor deposition, painting, along with finishing produced by machinery. A corporation that uses metal finishing on almost all its products is the Ingersoll Rand. The I-R has been a major supplier of power tools since 1871 (IR, 2012). Simon Ingersoll invented the first rock drill which was used in the building of the Hoover Dam and the sculpture of Mount Rushmore. Each individual metal part that went into the production of that rock drill and every power tool manufactured since has had its surface finished. Metal water buckets are galvanized with a zinc process to prevent the water from rusting the bucket. Jewelry’s metallic surfaces, medical instruments, mechanical tools, electronics all have finished surfaces. If you think of the many metal surfaces in your home and office, they have all been finished in some manner to provide corrosion, wear, tarnish, chemical or electrical resistance; electrical conductivity or reflectivity and appearance.
Environmental Impacts
In addition to the effluent waste water flow, these metal finishing sources can have a negative impact on the environment through several different mediums. Electroplating can introduce Hexavalent chromium into the air which can have a delayed impact on employees, animals, and civilians who come in contact with this effluent flow. In addition to the air impacts, Hexavalent chromium can exist in the shallow soil long after metal finishing processes have ceased. This can be spread through ingestion of animals who have come in contact with the soil or direct contact. Hexavalent chromium is a well documented carcinogen and plays a vital role in proper planning for effluent flows in this industry. The presence of one or multiple RCRA 8 metals (Ag, Ba, Cd, Cr, As, Pb, Hg, Se) is also highly plausible in either a solid or airborne medium. All of these poisonous or carcinogenic metals can exist in the air or soil and can have chronic or acute effects on people that ingest, absorb, or inhale. These metals are frequently the focus of environmental investigations and can inflict high remediation costs due to their presence in air, soil, or groundwater.
Regulations
40 CFR Part 433 Subpart A (EPA, 1983) regulates effluent water from industries that use processes to finish metals. There are 119 toxic organics listed in §433.11(e) which are regulated in quantifiable sums > .01 mg/L. The discharger must test their effluent to determine if their processes create waste from any of these Total Toxic Organics (TTO). Best Practicable Control Technology (BPT) or Best Available Technology (BAT) must be utilized in regards to effluent limitations on up to twelve pollutants or pollutant properties (U.S., 2012). Cyanide is addressed as a separate pollutant altogether. Additionally, Pretreatment Standards for Existing Sources (PSES) apply for nine effluent pollutants. There are also standards that cover New Source Performance Standards (NSPS) as well as Pretreatment Standards for New Sources (PSNS). The common pollutants addressed in all effluent are Cadmium, Chromium, Copper, Lead, Nickel, Silver, Zinc, Cyanide and TTO. Three more considerations that need to be addressed prior to discharge are Oil and Grease, TSS and pH. In NYS, the Department of Environmental Conservation has EPA approved programs that dischargers must follow (DEC, 2007).
Pretreatment Standards
Pretreatment of wastewater before discharging the water to a POTW is required. Because the water is treated prior, the industry user is considered an indirect discharger. This protects the POTW from wastes created by the industry that could cause damage or danger at the POTW. It also places the responsibility for the costs of treating the water onto the business creating the waste instead of the municipality that is operated on public tax money. Some pollutants could interfere with the operation of the POTW. Another potential problem is that the waste being discharged may not be a common pollutant that the POTW is set up to monitor for. Pretreatment also improves the POTW’s ability to recycle wastewater and sludge. The indirect discharger must abide by limits of pollutant levels set by both the federal, state and local governments as well as the POTW. Normally, the federal standards are the guidelines used by other agencies or municipalities. Title 40 Part 403 outlines the general pretreatment standards for existing and new sources of pollution.
Metal finishing facilities’ pretreatment standards are specifically controlled under 40 CFR Part 433. Some pollutants are prohibited; these are ones which could create an explosion, cause corrosive damage, obstruct flow, introduce excessive heat or release toxic gases. In lieu of testing for Total Toxic Organics, the owner or responsible person may sign a statement in the comments section of the discharge monitoring report (DMR) stating that to their knowledge, no concentrated dumping of toxic chemicals has occurred since the last DMR. Under this statement, when monitoring samples are needed to remain in compliance, only analysis for the pollutants that would be reasonably suspected need to be done. If certain pollutants are added to or are produced by the process of the individual business, they can be reasonably accurate in assuming what goes into the process must come out.
There are two types of technology-based limitations that are addressed in the regulations for metal finishers. The first one is Best Available-Based Limitations. These limits are used for businesses that may be older and not equipped with technology suited to pre-treat as well as newer facilities. Therefore, the economics of updating the facility are factored. The financial hardship of upgrading may be great enough to close the business. The goal of the regulations is to protect the environment and the POTW within reasonable efforts on the part of the businesses; it is the best equipment available to them. The second, is Best Practical Technology which is used for newer facilities that are utilizing the most recent equipment currently available. BPT has additional pollutants to test for that BAT does not; oil and grease, total suspended solids and pH. While this may not seem justified to allow older facilities to not take certain pollutants into consideration, these facilities may have larger maintenance on their equipment as the FOG and TSS not being considered in the beginning of the process. This will lead to the need to replace equipment sooner, at which time the newer technology will provide for the removal of these pollutants.
Another set of categories for dischargers is pre-treatment standards for new (PSNS) and existing (PSES) facilities. Those effluent limits are the same as in Table 1 with the exception of the limits for Cadmium in new facilities has been decreased to 0.11 mg/L daily and 0.07 mg/L average monthly. The PSES also does not set limitations on FOG, for the same economical factors stated for BAT.
Table 1 BAT and BPT Discharge Limits
Title 40 Section 433.13 and 14 |
||||
BAT Discharge Limits |
BPT Discharge Limits |
|||
Pollutant |
Daily Max mg/L |
Monthly Max Avg. mg/L |
Daily Max mg/L |
Monthly Max Avg. mg/L |
Cadmium |
0.69 |
0.26 |
0.69 |
0.26 |
Chromium Total |
2.77 |
1.71 |
2.77 |
1.71 |
Copper |
3.38 |
2.07 |
3.38 |
2.07 |
Cyanide A* |
0.86 |
0.32 |
0.86 |
0.32 |
Lead |
0.69 |
0.43 |
0.69 |
0.43 |
Nickel |
3.98 |
2.38 |
3.98 |
2.38 |
Silver |
0.43 |
0.24 |
0.43 |
0.24 |
Zinc |
2.61 |
1.48 |
2.61 |
1.48 |
TTO |
2.13 |
2.13 |
||
Oil & Grease |
52 |
26 |
||
TSS |
60 |
31 |
||
pH | 6.0 – 9.0 | 6.0 – 9.0 | ||
* Amenable to alkaline chlorinization as opposed to Total Cyanide |
Source: Title 40 Section 433.13 and 14
Sampling
Appendix E of Part 403 gives directions on two types of sampling procedures; composite and grab methods. Composite entails using samples taken over the course of a 24-hr span that will be mixed together in order to get a reading of the average pollutants. Grab samples are individual samples. Samples of both influent and effluent water should be taken. The influent samples allows the lab providing analysis for how much treatment additives and detention time may be necessary for the WWTP to successfully remove the various pollutants. The effluent samples determine if the water is under the limits allowed for water being discharged.
Application Process for SPDES Permit
Under the Clean Water Act, the federal government of the U.S. enacted the National Pollutant Discharge Elimination System. This set of regulations control all discharges of water, whether it be stormwater or discharges to municipal storm/sewer systems. New York State operates an EPA approved program, the State Pollution Discharge Elimination System (SPDES). There can be general permits, which cover stormwater or an industrial permit, which covers both stormwater and point source discharges. The metal finishing industry falls into Sector AA for Fabricated Metal Products. Part of the requirements for having a SPDES permit is the development of a Stormwater Pollution Prevention Plan (SWPPP). The SWPPP must have a site description that includes a site map, a section on spills and leaks and summary of potential pollutant sources. Areas for metal finisher businesses to consider when creating their SWPPP may include:
- Spills or leaks from containers of chromium, toluene, pickle liquor, sulfuric acid, zinc and other priority or hazardous chemicals
- Storage of raw materials, paints, empty containers, corn cob, chemicals, scrap metals, outdoor manufacturing, grinding, cutting, degreasing, buffing, brazing, spent solvents, sludge, shavings, ingots pieces, refuse and waste piles.
Stormwater controls such as good housekeeping, spill prevention and response procedures, inspections and comprehensive site compliance evaluations must be part of the SWPPP. While process wastewater is a major consideration, it is also critical to control pollutants that could be accidentally spilled or picked up by stormwater because this water may not be separated from piping that carries sewer water to the local POTW. Some areas of concern in the metal finishing industry are the following:
- Metal fabricating areas – kept clean and dry
- Storage areas for raw metal – measures to prevent spill or leakage of materials
- Receiving, unloading and storage areas – clean up procedures
- Storage of equipment – covers, storing indoors, clean up of pollutants if outdoors
- Metal working fluid storage areas – describe and implement measures for storage
- Cleaners and rinse water – control/cleanup (sandblasting, solvents, recyclable wastes)
- Lubricating oil and hydraulic fluid operations – leak detection, overflow, controls
- Chemical storage areas – prevent stormwater contamination, accidental spillage
The SPDES permit gives guidelines for which certain pollutant levels must be reported to the NYS DEC on an Annual Discharge Monitoring Report. Table 2 addresses these pollutants and their respective limits.
Table 2 Sector AA – Benchmark Monitoring Requirements
Sector AA – Benchmark Monitoring Requirements |
||
Pollutant of Concern |
Analytical Method |
Benchmark Monitoring Cut-Off Concentration |
Fabricated Metal Products Except Coating (SIC 3411-3471, 3482-3499, 3911-3915) | ||
Total Nitrogen |
EPA 350.1, 351.2, 353.2 |
6 mg/L |
Total Recoverable Aluminum |
EPA 200.7 |
750 ug/L |
Total Recoverable Iron |
EPA 200.7 |
1 mg/L |
Total Recoverable Zinc |
EPA 200.7 |
120 ug/L |
Source: NYS DEC SPDES Multi-Sector General Permit (GP-0-06-002) page VIII.AA – 3
These limits are not to be confused with the limits set forth for the pre-treatment limits for discharge to a POTW. These are separate guidelines and both set of limits must be followed. These requirements are what the NYS DEC expects to be monitored prior to discharge to either a NYS body of water or to a stormwater/sewer system.
After the SWPPP has been developed, and before discharging, a Notice of Intent or Termination (NOIT) must be filed with the NYD DEC. This form contains information about the company. The NYS DEC can use this information to know what to expect from this particular site. They will in turn mail out forms needed to be returned to the DEC at various intervals depending on the individual business. One of the forms required to be returned is the Annual Discharge Monitoring Report (DMR). The above pollutants of concern will be listed on the DMR. Other factors may be mass loading, concentrations, sample type and frequency of sample. If there are concentrations above the limits, explanations are to be made in the Comments section.
Typical Wastes from Metal Finishing Processes
Each operation is unique in exactly what process they are performing and what the end product is. The system by which metal finishing follows has similar sequence. There are rinse tanks, ventilation systems, acid cleaners/acid etchers, and alkaline cleaners (Fister, 2010). One of the largest expenses comes from cleaning/rinse water. After each process, the metal is cleaned with water. Table 3 shows the amount of pollutants for common processes used in metal finishing (EPA, 1982). These pollutants end up in the wastewater.
Table 3 Typical Waste Characteristics of Metal Finishing Operations
Unit Operation |
Waste Characteristics |
Total # of Pollutants |
Total # of In-organic Waste |
Total # of Organic Waste |
||||||
Inorganics |
Organics |
|||||||||
Common Metals |
Precious Metals |
ComplexMetals |
Cr6 |
Cyanide |
Oils |
Solvents |
||||
Cleaning |
1 |
1 |
1 |
1 |
1 |
1 |
1 |
7 |
5 |
2 |
Heat Treating |
1 |
1 |
1 |
1 |
4 |
2 |
2 |
|||
Electrochemical Machining |
1 |
1 |
1 |
1 |
4 |
2 |
2 |
|||
Tumbling |
1 |
1 |
1 |
1 |
4 |
3 |
1 |
|||
Burnishing |
1 |
1 |
1 |
1 |
4 |
3 |
1 |
|||
Electroplating |
1 |
1 |
1 |
1 |
4 |
4 |
0 |
|||
Electroless Plating |
1 |
1 |
1 |
1 |
4 |
4 |
0 |
|||
Conversion Coating |
1 |
1 |
1 |
1 |
4 |
4 |
0 |
|||
Etching (Chemical Milling) |
1 |
1 |
1 |
1 |
4 |
4 |
0 |
|||
Polishing |
1 |
1 |
1 |
3 |
2 |
1 |
||||
Machining |
1 |
1 |
2 |
1 |
1 |
|||||
Grinding |
1 |
1 |
2 |
1 |
1 |
|||||
Impact Deformation |
1 |
1 |
2 |
1 |
1 |
|||||
Pressure Deformation |
1 |
1 |
2 |
1 |
1 |
|||||
Shearing |
1 |
1 |
2 |
1 |
1 |
|||||
Other Abrasive Jet Machining |
1 |
1 |
2 |
1 |
1 |
|||||
Electrodischarge Machining |
1 |
1 |
2 |
1 |
1 |
|||||
Anodizing |
1 |
1 |
2 |
2 |
0 |
Source: National Service for Environmental Publications Table 4 – 2 pg. IV – 4 (EPA)
Wastewater Contaminated by Metal Finishing
Each site has unique properties which require analysis of the components in the process water that will be sent for treatment prior to discharge. Even within like industries or even industries that have the exact process and are owned by the same company will still have variations. Therefore one of the most important processes is the initial analysis, and careful monitoring thereafter. Depending on fluctuations in the process giving off waste water will dictate how often monitoring needs to be done. In an ideal situation, the WWTP will run almost at an automatic procedure, however it is wise to test the water periodically and record the results to ensure compliance with the limits.
Treatment Processes
Metals in wastewater stemming from metal finishing are most often soluble and or suspended in the water. In order to remove the metals that are basically floating in the water, the goal is to get the metals to become insoluble and then attract to each other so larger aggregated materials start to form. In order to turn the metals from soluble to soluble, a couple different directions can be taken. The solubility of metals are pH dependent. The first step is to use chemical precipitation. Metals can be precipitated out as hydroxides, carbonates or sulfides. Generally, hydroxide precipitation is the direction that most metals react best as. The metals in the water are atoms or groups of atoms that have electrical charges. These “ions” of metal can be cationic (positive), anionic (negative) or neutrally (nonionic) charged (EPA, 2000). Next, coagulation and flocculation is utilized. Polymers are often used to coagulate metals. The polymers act as bridges between the metal ions, grouping them together. Flocculation is a continuance of the coagulated materials into bigger clumps. The water then goes through clarification. Because the pH is adjusted greatly during the treatment process, the pH is balanced before discharge. Finally, the sludge is dewatered. The water from the sludge is sent back through the process due to the possibility of particles passing through at this stage. This is a very generic description of the process. Each wastewater from metal finishing is very unique.
Contaminants Other Than Metals
In the metal finishing industry, most often there is oil and grease involved in the wastewater. Generally, in many metal finishing processes, oil is used to keep the metal cool or lubricated to prevent wear and also to help machining to glide on the metal being worked on. On average, 10,000 to 20,000 mg/L can be in wastewater of some metal finishing industries (WEF, 2008). Individual pollutants and levels are site specific. Some general levels of in wastewater from a typical metal finishing business are as follow:
Table 4 Typical Wastewater Demands
Biochemical Oxygen Demand |
Total Suspended Solids |
Chemical Oxygen Demand |
Total Organic Carbon |
Total Kjeldahl Nitrogen |
3,000 – 4,000 mg/L |
2,000-3,000 mg/L |
20,000 – 30,000 mg/L |
7,500 – 10,000 mg/L |
100 – 200 mg/L |
Source: Industrial Wastewater Management, Treatment and Disposal, pg. 134 3rd Edition, WEF Press. 2008
Oils and greases are usually the first pollutant to be removed. They tend to cause maintenance problems with equipment down the line if allowed to stay. The treatment of oily wastes is first by means of segregation, then gravity separation followed by skimming. Emulsifying the oils helps float the oils to the surface.
Cyanide
While each site is different, there are known values for handling average concentrations of various metals. Whenever cyanide is in the mix, the water is always treated to eliminate the cyanide as the first metal to be removed (Holtzman, 1994). Ideally, if possible, cyanide streams should be kept separate from other waste streams. As a preliminary test, the lab at the wwtp should find out how much total cyanide and how much amenable cyanide is present in the water (WEF pg 385). It is done in a two step process called alkaline chlorination. The first process raises the pH to 9.5 to 11. Chlorine gas is often used, and another chemical used is sodium hypochlorite to change cyanide to cyanaogen chloride, then quickly to cyanate when it is amenable cyanide. Then the second step changes the cyanate into carbon dioxide and nitrogen gas the pH lowers to between 8.5 and 9. Cyanide is precipitated out using oxidation rather than later on with the other metals using hydroxides because many metals will create strong complexes with cyanide (Armenante). When the cyanide is not amenable, it is as a complex with another metal such as iron, chromium, or nickel.
Hexavalent Chromium
Another metal that needs to be treated in this fashion is Hexavalent Chromium. For this process, the pH is lowered to the acidic side of the pH scale to 2.5. This is done by adding Sulfur dioxide to the mix. This changes the +6 Cr to Trivalent Chromium, which can then continue on with the waste water and be treated with the other metals.
Other Metals
Most metals become insoluble at higher, more alkaline pH. At lower pH, metals are soluble. To get them to precipitate and settle, they need to be put into solid form. To aid this process, coagulants are added. These additives get the metals to attract to each other, which helps to get the metals to settle. In this first part of the process of treating the metals in group-like manner, the pH is raised back up to 6 to 6.5. Polyaluminum is a common metal reducer used to coagulate the metals. The water is then brought up to a pH of 7.5 to 8 by the addition of Sodium hydroxide. Finally, the last tank the pH is raised to 9, although there are cases that need the pH to be raised as high as 11 at this point. Flocculants are added, which allow some of the wastes to float, where they will be skimmed off. The remaining metals settle and are removed to a sludge tank. The sludge gets thickened and then is transferred to another piece of equipment that will dewater it. Depending on the type of metals removed, the sludge disposal may need to be transported to a hazardous waste disposal site.
The water that has been through all the precipitating, settling and flocculation processes then goes through a filter. The filter is usually either sand or carbon, and sometimes both are used. When the sensors pick up on either low head pressure or that particles are passing through the filter, the filter is then backwashed. The backwash water goes back to the beginning, as some metals may be contained in the backwash. After the water clearly goes through the sand/carbon filter(s), it goes to a tank where the pH is adjusted. At this point, it is ready to be discharged.
Table 5 Typical Concentration Ranges of Metals in Metal Finishing Wastewater
Typical Initial Ranges of Metals and the pH or Ion that will Precipitate the Metals |
||||
Pollutant |
pH that will Promote Precipitation |
Typical Range of Mean Concentrations mg/L |
Concentration of Metal Ion |
|
Hydroxide mg/L |
Sulfide mg/L |
|||
Cadmium |
9.0 – 11.0 |
0.28 |
2.3 x 10-5 |
6.7x 10-10 |
Copper |
7.0 – 8.0 |
12.6 |
2.2 x 10-2 |
5.8 x 10-18 |
Lead |
8.5 -9.0 |
0.33 |
2.1 |
3.8 x 10-9 |
Nickel |
9.0 – 11.0 |
15.5 |
6.9 x 10-3 |
6.9 x 10-8 |
Silver |
9.0 – 12.0 |
Trace |
13.3 |
7.4 x 10-12 |
Zinc |
8.0 – 8.5 |
12.5 |
1.1 |
2.3 x 10-7 |
Sludge
During the wastewater treatment process, a contaminated sludge is generated which can contain FOGs, metals and other compounds. This sludge must be removed from the facility, typically through a third party, for final disposal. To start off the disposal process, the sludge must first be sampled for basic waste parameters such as ignitability and corrosivity. In addition to these waste parameters, the EHS team must also collect and submit Toxicity Characteristic Leaching Procedure (TCLP) samples. The waste parameters are used to monitor the effect of storing the soil in a landfarming environment to ensure safe, permanent disposal. The TCLP sample replicates rain water of an average pH percolating through the surface soil and contaminated sludge in an effort to study the potential effects of water movement versus contaminant mobility. If the TCLP samples come back under the action level that is specified by the state, meaning that the samples did not “leach” a sufficient amount of materials (metals in this case), then there is no additional stabilization requirements. If the samples come back showing that the sludge would leach contamination to down-gradient locations due to naturally occurring rainwater, then additional stabilization is required. Stabilization methods include mixing Portland cement, lime, bentonite, or a combination of the 3 with the contaminated sludge. Disposal facilities, such as the one in Robstown, TX, may also choose to use a proprietary blend of stabilization material such as “Enviroblend”. Once the sludge has been classified as either hazardous or non-hazardous waste, the process can begin of transporting it. If the sludge has been deemed non-hazardous it can typically be disposed of at a number of landfills. If the sludge has been deemed hazardous or needs stabilization, the choices are limited on where you can dispose of it. Typical treatment fees for a chromium contaminated sludge can range from 200-250 dollars per ton. This fee includes the cost of stabilization. If the concentrations are extremely high, it is possible that additional measures will have to be taken to stabilize the sludge. Additional stabilization can incur longer transportation fees and higher rates per ton of material. In the end, the sludge will be removed from the wastewater treatment facility for disposal. The path that the sludge takes towards final disposal will vary from facility to facility
Wastewater Management Strategy
Wastewater Reuse
Designing processes that can reuse water within the facility is an efficient way to save time and money. A great example would be to clean up process water to a level that would be considered satisfactory to use for rinsing. This quality could be achieved by a number of processes such as Koch Membrane System’s tubular, ultrafiltration membranes (Koch). These membranes can remove FOG and heavy metals so that the effluent flow may be safely utilized in other facility processes. This process works by first establishing cleanup criteria for your effluent flow. By establishing a internal system of standards to which wastewater can be cleaned up, an EHS manager can determine what operations can use the water based on the standard.
A small process, or group of processes can be implemented to assist with the wastewater reuse. These processes would operate upstream of the treatment plant and would cycle the majority of wastewater back into the facility as treated water to be used in select operations. These processes may remove a particular contaminant or group of contaminants to make the wastewater stream acceptable for the appropriate internal function. These processes can cycle back a large amount of water, but still produce some wastewater to be sent to the treatment facility. Addition of these systems also brings about additional maintenance costs and monitoring for the equipment. Consideration must be taken to weight the costs benefits over time of installing a wastewater recycling system versus the upkeep and construction of the system.
Another example of a water reuse process would be capturing storm-water from the throughout the facility boundaries. LEED architecture designs incorporate storm-water collection into structures and utilize this resource when there are no strict restrictions on water parameters. Collecting storm water to use in rinsing processes and sanitary facilities takes advantage of an existing resource and reuses it within the operating processes. Designs can also be incorporated into existing facilities which can affect permitting and reduce operational costs. Organizations such as the National Onsite Wastewater Recycling Association (NOWRA)provide knowledge to companies that are wanting to make best advantage of their wastewater (NOWRA). For a large metalworking facility that requires multiple rinse stations, this is a great opportunity for wastewater reuse.
Reducing Operational Costs
There are various ways in which a metal finishing organization can reduce operational costs. One of the first ways to optimize many processes within an facility is to look carefully at the use of water. Reductions to water intake and minimization of wastewater production is of course the most obvious methods. Identifying ways to reuse fresh water or slightly used water can also present a great opportunity to drive down costs. Reductions to wastewater output will affect the overall design of a wastewater system a lot of designs are based off influent flow volumes and the area required to lower concentrations of contaminants. The intelligent use of water in a closed system will provide the greatest cost reductions over time. Researching alternative chemicals to use within the metal finishing process is another method to reducing operational costs over time. Although this process requires investment on the front end, finding a chemical that more effectively reduces contaminants in your wastewater treatment facility or can eliminate a contaminant completely can have enormous financial benefits on the back end. Increased efficiency of contaminant removal can have positive effects on applicable permits and regulations, sampling methodology for monitoring, agency involvement in business affairs, potential legal/liability issues, and exposure concerns to workers. All of these processes incur a cost to the organization and any reduction can be seen as a great benefit over time. Normalizing the waste stream can also have a beneficial impact on costs. By reducing the amount of variability in the wastewater, we can eliminate the need for equalization tanks and additional steps in the treatment process. Modification of the order of events within the operational process can produced this desired effect if possible.
There are many ways to reduce costs associated with wastewater treatment. Optimization of processes, selection of chemicals, treatment facility design, and resource usage all intertwine and add to the total cost of wastewater handling at a facility. The proper management of these details can create huge saving to the facility owner as well as increased sustainability and profitability in the future. Sustainability and profitability is marketable to consumers, shareholders, and prospective employees as selling points for interest in the company. As EHS becomes more integrated into companies, more focus will be placed on details such as these as a way to increase the bottom line.
Conclusion
The metal finishing industry deals with a variety of complex issues from a wastewater standpoint. The contaminants associated with the industry and the concentrations in which they are emitted to the environment can create complicated problems that must be solved by skilled EHS professionals. Careful consideration must be taken for the health and environmental effects for present exposure and also potential future exposure pathways. Source reduction, cost reduction, and water recycling have proven to be successful foundations for wastewater management in this industry. A thorough understanding of the best practices, regulations, and efficient technologies mentioned above will provide a manager with an excellent foundation with which to begin solving these issues.
Works Cited
Armenante, P. M. (n.d.). Precipitation of Heavy Metals. Retrieved February 12, 2012, from http://cpe.njit.edu/dlnotes/CHE685/Cls06-2.pdf
DEC, N. (2007, March 28). SPDES Permit. Retrieved February 24, 2012, from New York State Department of Environmental Conservation: http://www.dec.ny.gov/docs/water_pdf/gp0601.pdf
EPA. (1982, August). Development Document for Effluent Limitations Guideline and Standards for the Metal Finishing. Retrieved February 4, 2012, from 2007_10_22_guide_metalfinishing_tdd-proposed.pdf
EPA. (1983, July 15). Environmental Protection Agency Code of Federal Regulations. Retrieved February 4, 2012, from Part Subpart A – Metal Finishing Point Source Category (48 FR 32485): http://edocket.access.gpo.gov/cfr_2010/julqtr/pdf/40cfr433.10.pdf
EPA. (2000, September). Wastewater Technology Fact Sheet – Chemical Precipitation.
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