Trivalent Chromium Plating Conversion Case Study Independent Plating, Worcester, Massachusetts

Similar documents
AESF Aerospace / Airline Plating Forum - Tulsa, OK.

Anodizing Reference Guide

Removing Heavy Metals from Wastewater

NO TARN 15. 5) Can be used on Silver AND Gold. Protects gold from blackening during shipping due to reaction with box chemicals.

Ion Exchange Softening

ABC CIRCUITS 10 Circuit Drive Circuit Town, IN SLUG CONTROL PLAN

An Ammonium-free, Acid. Zinc/Nickel (12-15% Ni) Process

Nickel Free Room Temperature Seal: an innovative and ecological process

Zinc Electroplating CHOOSING THE BEST PROCESS FOR YOUR OPERATION

Metal Rescue Rust Remover Technical Data

Successful Pollution Prevention Strategies in a Zinc Die-Casting Plant

Cooling Tower Sidestream Filtration A Green, Proven Cost Reduction Technology

Metal Ion + EDTA Metal EDTA Complex

TECHNICAL DATA SHEET DURO HARD CHROME PLATING PROCESS

Water Treatment & Purification Chemicals

The Empirical Formula of a Compound

Metal Finishing: How to Save on Alkaline Cleaners, Acids, and Rinse Water May 10, 2011 Dave Fister, Senior Staff Engineer

Environmental Technology March/April 1998

RECOVERY and PURIFICATION of NICKEL SALTS and CHROMIC ACID using the RECOFLO SYSTEM

Spray Nozzles. Spray Control. Spray Fabrication. Spray Analysis. A Guide to Optimizing In-Tank Agitation and Mixing Using Eductors

INDUSTRIAL ROOFING CASE STUDY: The Advantages of Aluminized Stainless Steel. Roof Installed:

The Electrical Control of Chemical Reactions E3-1

Troubleshooting Your RO

Greening Our Future By Educating Tomorrow s Workforce. Module 2: Lean Manufacturing and the Environment

Wastewater Reuse. Typical treated wastewater is:

DURAPOSIT TM SMT 810 Electroless Nickel

& CLEANING GUIDE MAINTAIN BEAUTY & PERFORMANCE

SurTec 650 Tri-Chrome Passivation of Aluminum

Iron and Manganese BACTERIA AND IRON AND MANGANESE

care & cleaning guide

Anodizing by Constant Current Density

Marina Bay on Boston Harbor Water-treatment system by OilTrap Environmental

Sulfites for Oxygen Control

Nine Industrial Scale V SEPs. Feed Tank V SEP. Feed Pumps (Three) Concentrate. Tank. V SEP Treatment System

Dentistry and the Environment

North American Stainless

Waste and Cost Reduction Techniques for Small Parts Cleaners

Making Point-of-Sale and Commercial Displays Safe for Retailers and Consumers

Chemical Fume Hoods. Environmental Health and Safety

Auditing a Printed Circuit Board Fabrication Facility Greg Caswell

HEXAVALENT CHROMIUM REMOVAL FROM INDUSTRIAL WATSEWATER BY CHEMICAL PRECIPITATION METHOD

COMPOSITE MESH PAD (CMP) DRY SCRUBBERS III TM ENFORCER III

Cellar Tech Containment Well Cellar Systems

Water Softening for Hardness Removal. Hardness in Water. Methods of Removing Hardness 5/1/15. WTRG18 Water Softening and Hardness

CATHODIC PROTECTION SYSTEM DESIGN

Crevice Corrosion on Stainless Steel Propeller Shafts

the runnerless types of molds are explained post molding operations are described the basic methods of applied decoration methods are examined

F The following spent

WATER CHEMISTRY AND POOL WATER BALANCE

Hazardous Waste Procedures. Faculty of Science University of Ottawa

Process Specification for the Anodizing of Aluminum Alloys

Austin Peay State University Department of Chemistry CHEM 1021 TESTING FOR ORGANIC FUNCTIONAL GROUPS

Solubility Curve of Sugar in Water

Building Electrochemical Cells

Emergency Showers and Eyewashes Mike Adkins Wednesday, October 31, 10:00-11:1511:15 a.m.

ACL 395 Resistivity Meter

Environmental Water Testing: Surface Water, Groundwater, Hard Water, Wastewater, & Seawater

Identifying Your Hazardous Waste

KODAK Developer System Cleaner and Neutralizer

QUALANOD SPECIFICATIONS UPDATE SHEET Nº 9 Edition page 1/5 COLD SEALING PROCESS

Best Available Technology for Sodium Hypochlorite Storage Tanks

PART 1 - INTRODUCTION...

INTRODUCTION WHAT ARE TRANSITION METAL COATINGS? WHAT IS THE APPEARANCE OF A TRANSITION METAL COATING PRETREATMENT?

Product Finishes Guide. More for your door than any other brand.

Atomic Structure. Atoms consist of: Nucleus: Electrons Atom is electrically balanced equal electrons and protons. Protons Neutrons

Test Methods for the Colour Fastness of Leather & Dyes. TFL Leather Technology Ltd. Quality and Environment February 2004 Version 1.

BHS CANDLE FILTER APPLICATIONS FOR CLARIFICATION / RECOVERY OF SOLIDS FROM CHEMICAL SLURRIES

North American Stainless

Introducing an All New Line of Cleaning Chemicals

Rubber-to-Metal Bonding

Properties of Acids and Bases

Water Efficiency. Water Management Options. Boilers. for Commercial, Industrial and Institutional Facilities. Boiler Water Impurities

Remediation of VOC Contaminated Groundwater

ECOAZUR BLUEWATER WATER PURIFICATION PLANTS

Structural Bolting. Notice the Grade 5 has a much smaller head configuration and a shorter shank then the A325 structural bolt. Rev.

WATER TABLE WINNERS!

Well Water Iron Removal Using Quantum DMI-65 Granular Filter Media

5.0 EXPERIMENT ON DETERMINATION OF TOTAL HARDNESS

Electrochemical Half Cells and Reactions

POOL SUNSHINE IONIZER MODELS SPD, SPD2 AND SPS INSTALLATION INSTRUCTIONS

North American Stainless

4 RECORDS STORAGE OPTIONS

Determining the Quantity of Iron in a Vitamin Tablet. Evaluation copy

Plastisol vs. Water-based Ink for Textile Printing by Mike Ukena

CHAPTER 5. OVERVIEW OF THE MANUFACTURING PROCESS

Self Assessment Exercise

Screw Plug Immersion Heaters

Chapter 5 - Aircraft Welding

GUIDELINES FOR LEACHATE CONTROL

North American Stainless

Removing Thallium from Industrial FGD Scrubber Water with Sorbster Adsorbent Media

Printed Circuit Board Recycling Methods

Characterizing Beauty Salon Wastewater for the Purpose of Regulating Onsite Disposal Systems

Safety Data Sheet Aluminium profiles Apply for alloys Sapa EN AW 6060, 6063, 6005, 6005A, 6082, yellow chromated, with or without powder coating.

ALLOY C276 DATA SHEET

Neutralizing an Acid and a Base

Cat S O SSM. Services. Understanding Your Results. Understanding Your: S O S Oil Reports S O S Oil Results S O S Coolant Reports S O S Coolant Results

Reuse of Alternative Water Sources for Cooling Tower Systems Two Case Studies Using Non-Traditional Water Sources

REVISION NO : 3 August 2010

Transcription:

Trivalent Chromium Plating Conversion Case Study Independent Plating, Worcester, Massachusetts Faced with new regulations restricting emissions of hexavalent chromium (hex-chrome) from various plating operations, and increasing requests from its customer base for products that are environmentally preferable, Independent Plating (Independent) decided to explore converting one of its plating lines from hexavalent to trivalent chromium. Such a conversion is consistent with Independent s overall approach, which relies on substitution and prevention as their principal techniques for toxics use reduction. Their philosophy emphasizes source reduction, drawing heavily on research and implementing new safer and greener alternatives. With a commitment to providing safer, high-quality metal finishing in an environmentally sound manner, Independent plans to continue its proactive approach to growth well into the future. Background Independent Plating is an employee-owned metal finishing company that has been in business since 1941. For more than 70 years, Independent has been finishing an array of primarily aluminum and stainless steel tubing and wire products for a variety of products from school furniture to high end retail displays to medical devices to law enforcement tools. Metal finishing processes conducted at Independent include zinc plating, electroless nickel plating, black oxide, nickel chrome plating, phosphating, pickling and powder coating. These processes contain various heavy metals, acids and other hazardous substances, which pose potential negative impacts on the environment and workers. Consequently, Independent s metal finishing operations are subject to many environmental and occupational regulations, including new emission standards recently finalized by the US Environmental Protection Agency 1. The specific processes used by metal finishers for various products are traditionally dictated by the demands of their customers. This often limits a finisher s choices when it comes to selecting the highest quality finish while reducing potential impacts on human health and the environment. Ten years ago Independent attempted to switch its nickel chrome line to 1 US EPA National Emissions Standards for Chromium Emissions from Hard and Decorative Chromium Electroplating and Chromium Anodizing Tanks 1 P age Fall 2012

trivalent chromium, but found that the technology available at the time did not achieve the quality their customers required. However, Independent continued to stay informed about new technological advances in metal finishing and, when customer demands for products with a lower environmental footprint began to increase, they made another concerted effort to find an alternative. Assessment of Trivalent Chromium Independent Plating took a systematic approach to exploring its options for implementing a trivalent chromium (tri-chrome) system. The first step was to conduct research into the technologies now available, and the experience of their peers with the various options. One area of particular interest to them was corrosion resistance. Because Independent primarily does plating on tubular products, they were concerned with assuring that their plating treatments minimized corrosion on the insides of tubes. Research - Independent spent considerable time researching different tri-chrome systems to decide which would best meet all of their needs as well as the needs of their customers. They paid particular attention to the uniformity and thickness of coverage and the color achievable by the various options, as well as ease of system maintenance and the level of support expected from the vendor. They visited several plating shops that are currently using various tri-chrome systems, to learn about the operational requirements of their tri-chrome lines and to get feedback from these platers about their experiences with various vendors. Based on this research, Independent identified the following benefits and challenges of converting to a tri-chrome system: Benefits of Trivalent Chromium Improved quality: superior throw, better coverage around holes, less burning and whitewash, easier cleaning. Need for color buffing is nearly zero. Increased throughput: larger load sizes are possible. Increased rack density possible Less hazardous waste generated. Lower cost of hazardous waste management Lower toxicity (hex-chrome is a carcinogen) Minimizes employee exposure: potential employee exposure to toxic air emissions reduced Less likely to trigger future regulatory restrictions Challenges with Trivalent Chromium Cost: implementation and chemical costs are higher than hex-chrome. Appearance; although generally acceptable, tri-chrome colors are not quite identical to hex-chrome Technical capabilities: tri-chrome is not capable of replacing every hex-chrome requirement and/or specification. Bath control: tri-chrome baths require increased testing and maintenance, and operate with higher current requirements Still contains very small amount of hex chrome in solution 2 P age Fall 2012

Decisions After six months of research, Independent chose three vendors for further consideration. They sent each vendor parts that represented a range of products with which they typically work to assess the uniformity and thickness of coverage achieved, as well as their ability to closely match the bluish color of hex-chrome plated parts. Eventually, Independent decided on the vendor that provided a sulfate-based electroplating system (PAVCO, Inc.). Important factors in this decision included consistency of coverage, ability to most closely match the color of their customer s parts, operating cost savings (the sulfate system uses approximately one half the electric energy required for the chloride-based system), and vendor support. Design Compared with hex-chrome, tri-chrome takes approximately three times as long, at a reduced electric current (i.e., 3 minutes at 50 ASF) to achieve the desired thickness. Independent was able to modify one of its plating lines for the tri-chrome installation in a way that allowed them to meet the requirements of their customers and get the proper thickness of coverage. Specifically, the process flow was redesigned by moving from a 1400 gallon tank (for the hexchrome system) to a 3500 gallon tank for trichrome (see Figure 1.1). The new tank was built in-house, which resulted in significant savings and allowed them to control the design and installation process. In addition, Independent was able to modify an existing line to run either hex-chrome or tri-chrome (see Figure 1.2), thereby cutting down on the time and costs of the project. This also allowed them to pilot the tri-chrome system without any interruption to service for their customers. 3 P age Fall 2012

4 P age Fall 2012

Equipment Specification Independent worked closely with PAVCO to choose the appropriate process operating and control equipment. Specifically, the choice of automatic amp meter feeder and bath filter was vital to assure consistent quality and uniformity of the new plating process, and reduced much of the guesswork in maintaining correct process parameters. Much of the equipment required for the new tri-chrome system (e.g., filters, rectifiers, etc.) was already available in-house at their Worcester facility, which helped keep costs down. Installation With the dedication and hard work of Independent s facilities staff and finishing line operators, installation of the new tank and equipment into the existing plating line went as anticipated and was completed without any interruption of service. The total time required to redesign the process flow and complete tank fabrication and installation was approximately 8 weeks. Training Independent worked closely with PAVCO to train its lab personnel and metal finishing managers. The new system uses a dual pump amp meter feeder for automatic bath make-up additions. It was essential for operators to know how to properly use the automatic ph and temperature controllers, and analyze the tri-chrome bath for contaminant drag out and build up in the tanks. Operators were also trained in use of the new rectifier settings to improve the current density of the tri-chrome process. Performance training focused on maximizing the throwing power of tri-chrome, visually inspecting parts to detect potential chrome burn (characterized by white or yellow spots on the plated surface) and modifying racking procedures to maximize rack densities. Overall, Independent found that their line operators required very little training to master the new tri-chrome system. Results Product Quality Upon implementation of the new tri-chrome system Independent immediately noticed a reduction in rejects associated with whitewash and chrome burning. With tri-chrome they were able to virtually eliminate the need for color buffing. In addition to the reduction in reject rate, the superior throwing power and coverage of the tri-chrome system resulted in improved quality. The key factor, however, has been their ability to closely match the color of final products required by their customers. This color matching allows customers to easily commit Typical product with nickel trivalent chromium plating 5 P age Fall 2012

to the switch from the hex-chrome plated parts to the new tri-chrome plated parts. Additionally, the increased throw of the tri-chrome bath means better plating coverage on part crevices, internal openings and penetrations, thus improving overall product quality. A unique capability of this new line is its ability to run a variety of parts through at the same time and to increase the overall racking density without fear of developing chrome burn. Although not yet realized due to the large size of parts currently being finished, Independent anticipates that they may be able to increase the number of parts per load by 15% or more once the size range of parts processed in this system expands. In addition, the superior rinsing characteristics of the tri-chrome system allow them to reduce most of the cleaning steps further improving process throughput potential. O&M Costs Independent has experienced increased costs associated with maintenance and analysis with the new tri-chrome line. The filters on the tri-chrome line turn over 3500 gallons of solution five times an hour, resulting in the need for frequent filter maintenance and cartridge replacement. In addition, although an automatic amp meter feeder is used for additions to the tri-chrome bath, analysis of the bath concentration and make-up needs to be performed twice daily (as opposed to the weekly analysis associated with the previous hex-chrome system). Impurities Trivalent chromium baths tend to be more sensitive to metallic impurities than hexavalent chromium baths. One of Independent s main concerns was its ability to minimize metal impurities, specifically iron, in the tri-chrome bath. They also needed to watch for a buildup of hex chrome, which can result from ionic conversion of tri chrome in the bath from the anodes. Impurities are removed from the Independent system using hydrogen peroxide as a precipitating agent followed by filtration. However, addition of too much peroxide in the bath can lead to an increase in sludge formation that impacts subsequent waste treatment steps. In addition, due to the configuration of the Independent line with hex- and tri-chrome baths running in parallel (see Figure 1.2), they were concerned about the possibility of hex-chrome carrying over into the trichrome bath. To reduce the potential for this New tri-chrome line showing movable isolation wall contamination they designed a movable isolation wall that was installed between the two tanks. 6 P age Fall 2012

Wastewater Treatment and Hazardous Waste Generation There are important advantages associated with converting from hex-chrome to tri-chrome. Trivalent chemistries use lower concentrations of chromium in the bath, generally 5-7.5 g/l of trivalent chromium compared to 130-225 g/l for hexavalent chromium. Therefore, much less chromium enters the wastewater treatment process. Potential exposure of workers to toxic chemistries is also significantly reduced. Moreover, the reduction step associated with converting the highly toxic hexavalent chromium to trivalent chromium in wastewater treatment process is not required. This eliminates the need for reducing agents like sodium bisulfate and additional acid for ph control, and significantly reduces the volume of sludge produced. In addition, anodes in hex-chrome systems deteriorate over time, creating an additional source of hazardous solids in the waste stream. The tri-chrome process produces approximately one-tenth the sludge volume of the hex-chrome system, which significantly reduces associated hazardous material handling and disposal costs. Comparison Data The following table summarizes key data associated with the two systems: Trivalent Chrome Hexavalent Chrome Chromic Acid (oz/gal) 1.15 30.73 Current/Duration 50 ASF for 3 min 150 ASF for 1 min Operating Temperature (range) 126 F (122 to 136 ) 105 F (86 to 122 ) Plating Time Per Part 20 seconds 80 seconds Treatment Chemical Costs: Sodium Metabisulfite Sodium Hydroxide Estimated Chemistry Costs per Square Foot of Part Plated Anode Equipment/Maintenance: Anode Replacement Filter Cartridge Replacement Automatic Pump Feeder Reject Rate N/A N/A $0.55/lb $0.55/lb $0.04 $0.02 Iridium-oxide coated titanium (40 x 65 ) 18-24 months Every 2 weeks Every 5 years Low (white wash and burning not likely) Lead 40+ years N/A N/A As much as 15% (tendency to white wash or burn) 7 P age Fall 2012

Conclusions Independent Plating has a philosophy of staying ahead of regulatory restrictions, responding to customer demands, and optimizing the safety of its occupational environment while continuing to maintain its competitive edge. With an emphasis on source reduction and relying heavily on researching and implementing new safer and greener alternatives, they have successfully demonstrated the ability to shift their nickel chrome plating line from the use of hex-chrome to tri-chrome. As they continue to work with customers to convert specific product lines to the new tri-chrome process, Independent has had no customer complaints with respect to color or coverage quality. Although the operational costs associated with tri-chrome are higher than those for hexchrome, Independent is finding that as they gain more experience with tri-chrome, its costs are still coming down. Moreover, improved product quality, reduced reject rate, and the increasing desire for green products among its customers is helping Independent gain an ever-moreimportant market advantage. Independent intends to increase its use of tri-chrome and other potential alternatives to hexchrome, with a goal of complete elimination of hexavalent chromium in the next several years. It is not a simple conversion, however, and requires the commitment and dedication of skilled operators and engineers to be successful. It also requires constant communication with customers to demonstrate that this safer process can produce the quality and reliability they demand. This is a challenge that Independent Plating has been willing to make for its employees, for its customers, and for the environment. To learn more about Independent Plating s metal finishing capabilities or to discuss how your facility might be able to implement similar process modifications to reduce your use of hexavalent chromium, contact Mike Nahorniak, General Manager, 508-756-0301 ext. 100, or mike@independentplating.com For more information about the Toxics Use Reduction Institute Industry Incentive Grants program, contact Pam Eliason, Industry Research Program Manger, at 978 934 3142, pam@turi.org or Joy Onasch, Small Business and Community Program Manager, at 978-934-4343, joy@turi.org. For information about the on site confidential technical assistance services provided by the Office of Technology and Technical Assistance (OTA), contact Bill McGowan, Technical Services Chief, at 617 626 1078 or william.mcgowan@state.ma.us 8 P age Fall 2012