Callidus Oxidizer Systems. Thermal and Catalytic Oxidizer Systems

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Callidus Oxidizer Systems Thermal and Catalytic Oxidizer Systems

Meet the Thermal Oxidizer Experts Wide Range of Applications Honeywell UOP Callidus is an industry leader in environmental combustion technology. We have provided incinerators for a wide variety of gas and liquid wastes including inorganic particulate, various acids and hardto-burn organic compounds. Our experience extends to development and implementation of Thermal Oxidizer systems for Fume, Tail Gas, Halogenated Waste, Bound Nitrogen, Catalytic Oxidizers and Downfired Incinerators including units with ratings of more than 400 MM BTU/hr. Fume Thermal Oxidizers Honeywell UOP Callidus Fume Thermal Oxidizer thermally treat organic fumes in air or inert gas streams at s between 1400 F and 1600 F. Destruction efficiencies typically range from 99 to 99.99 percent. Catalytic Oxidizers Our Catalytic Oxidizers can be used in cases where the organic level is low and the fume stream is free from dust or substances potentially poisonous to the catalyst. Catalytic oxidation is generally carried out at 550 F to 850 F and requires substantially less fuel than thermal systems. Fume Thermal Oxidizer Typical Equipment Low emissions Ceramic fiber operation Burner management system Stack VOC streams Process vents Pharmaceutical vents Dryer exhausts Typical Installation 5 to 100 MM BTU/ hr 1 second residence time 1500 F Destruction efficiencies greater than 99.99 Tail Gas Thermal Oxidizer All of our products - Burners, Flares, Selective Catalytic Reduction systems and Thermal Oxidizers - are engineered and designed by combustion experts who have years of experience and are focused on customer satisfaction and emission compliance. Dedication to our customers is proven by the performance of our thermal oxidizer group. The engineers in this group are second to none in oxidizer experience and technical capabilities. We have been involved in the successful design, fabrication, and startup of hundreds of thermal oxidizers worldwide. We Pride Ourselves on Quality Our manufacturing facility employs the highest standards in the industry. Like many companies, our manufacturing techniques use state-of-the-art ; but, what truly sets us apart is our people. We take great care to ensure that highly trained individuals perform our special requirements. Ongoing and regularly scheduled training through our research and development group assures that a high level of quality is maintained. Leading the Way With Engineering Excellence Honeywell UOP Callidus focuses on meeting each customer s individual requirements, resulting in a custom-designed solution for every project. On average, each engineer has 15 years experience designing thermal oxidizers. Advanced Manufacturing and Fabrication Capabilities Upgrading our manufacturing and fabrication facilities is an ongoing process, and our facilities employ the latest manufacturing practices and. As a global leader in the thermal oxidizer market, much of our fabrication occurs in strategic locations around the world while proprietary items percent may be required for some organic wastes. This is achieved by the oxidizer at a higher with minimal auxiliary fuel. Waste heat boilers or hot oil heaters can be used downstream to recover heat for other plant operations. Tail Gas Thermal Oxidizers Tail Gas from Sulfur Recovery Units contains a variety of sulfur compounds, which are destroyed in our Tail Gas Thermal Oxidizer. Typical oxidizing s vary from 1200 F to 1500 F, with s of 0.6 to 1.0 second. System designs for both natural or forced draft are available. Generally, regulations require H 2 S in the flue gas to be 10 ppmv or less; but in certain cases, levels as low as 2 ppmv can be achieved. Low emissions Castable or brick Natural draft/ forced draft (optional) Stack Sulfur plant tail gas Carbon black tail gas Refineries Natural Gas Processing Plants 20 to 150 MM BTU/hr 1 second residence time 1200 F-1500 F 9.5 MM BTU/hr fume incinerator Our quality assurance personnel thoroughly inspect each assembly prior to shipment, thus reducing installation, and our fabrication and manufacturing are certified ISO 9001:2008 in the USA and China. are fabricated in our own facilities. This approach makes good economic sense, and provides you the best value for your combustion system. 20 MM BTU/hr sulfur plant tail gas incinerator 8 MM BTU/hr brominated waste 35 MM BTU/hr downfired system 15 MM BTU/hr fume incinerator 22 MM BTU/hr tail gas unit

Downfired Thermal Oxidizer Systems Halogenated Waste Thermal Oxidizer Systems Thermal destruction of aqueous or organic waste We have extensive experience in halogenated organic waste oxidation. streams containing inorganic or organic alkali The most common halogen is chlorine. Thermal oxidation of chlorinated metal salts requires that the thermal oxidizer be hydrocarbons produces hydrogen chloride gas (HCl) and some free downfired to prevent accumulation of molten chlorine, which must be removed. The quantity of HCl in the flue gas salts in the oxidizer furnace. Because molten determines whether a single or two-stage HCl removal system is used. salts tend to destroy, our design Either an HCl absorber or a caustic scrubber is used when a small quantity minimizes salt contact with lining, of HCl is present. A two-stage system is often used to reduce caustic which improves life. usage when the flue gas contains a significantly large quantity of HCl. Particulates entrained in the flue gas are removed by either a wet or dry flue gas clean-up system depending on the required emissions rate. In our wet system, salt or ash-laden flue gas Honeywell UOP Callidus Halogenated Waste Thermal Oxidizer Systems are capable of destruction efficiencies up to 99.99 percent. Operating s can range from 1500 F to 2200 F with s of 1.0 to 2.0 seconds depending on the destruction efficiency required. from the oxidizer first enters the quench system located directly below the thermal oxidizer. Here the hot gas is quenched to its adiabatic saturation by water injection or by a Callidus high efficiency submerged quench system (patent pending). Then, the saturated flue gas flows through a wet venturi scrubber and/or WESP (Wet Electrostatic Precipitator) before being sent to a packed column scrubber, if required, or vented to the atmosphere through a stack. In the dry system design, flue gas from the oxidizer is typically cooled by air and/or water injection before being sent to a baghouse or an electrostatic precipitator for particulate removal. Destruction efficiencies greater than 99.99 Downfired unit Downfired Thermal Oxidizer Low emission Low porosity brick Stream Ethylene plant blowdown Caustic waste streams Chemical plant 20 to 80 MM BTU/hr Halogenated Waste Thermal Oxidizer Medium intensity High alumina brick HCl recovery/ scrubber Stream PVC plant vents VCM waste liquids Pharmaceutical vents Bromine liquid wastes Chemical plant 10 to 50 MM BTU/ hr 1800 F Halogenated Waste Thermal Oxidizer percent are routinely achieved for most organic waste components at s of approximately 1800 F. Particle matter emission Adiabatic quench Particulate removal 1650 F-1800 F rates may vary from as low as 0.005 to 0.08 grains/dscf, depending on the particle removal selected to meet the customer s requirements. denoxidizer/tail gas unit 80 MM BTU/hr low NOx system

The Best in Design, Quality, Performance and Delivery Low NOx denoxidzer Systems Thermal oxidation of nitrogen-bearing wastes require a specialized combustion approach. Single-stage combustion of these wastes can produce NOx emissions in excess of those allowed by most regulatory agencies. To maintain NOx emissions within acceptable limits, Honeywell UOP Callidus uses a three-stage combustion process to destroy these wastes. The waste is burned in the first stage under substoichiometric, or reducing conditions. The high s and lack of oxygen in the first stage cause the nitrogen-bearing compounds to form elemental nitrogen rather than NOx. In the second stage, flue gas from the first stage is cooled to approximately 1400 F by injection of water, steam, or cooled recycled flue gas. The combustion process is completed in stage three where the flue gas is oxidized at a of 1700 F to 2000 F with excess oxygen present. NOx in the final flue gas typically ranges from 80 to 200 ppm, depending on the waste composition. A destruction efficiency of 99.99 percent can be achieved for most compounds. Three stage combustion system at Honeywell UOP Callidus research facility Low NOx Thermal Oxidizer High intensity Brick lined furnace Three stage process Ammonia vents Acrylonitrile vents Nitrogen bound organic wastes Representative Installation Petrochemical plant in India 10 to 60 MM BTU/hr 2200 F/1600 F s We Exceed the Expectations Quality assurance and customer satisfaction are our top priorities. Each step of a project is reviewed to meet or exceed our customers requirements and standards. Where applicable, is pre-assembled and tested. Fabrication is accomplished either in-house or by certified, experienced, and our rigorous quality inspection program is evident by our ISO 9001:2008 certification. Unequaled Research and Development Our industrial scale Thermal Oxidizer R&D facility is fully instrumented and utilizes process control and data logging systems. The facility is devoted to research and development of new products, new combustion processes, improvement of existing processes, and problem-solving efforts. The center also serves as a research facility for regulatory agencies as well as private clients. The Thermal Oxidizer R&D facility currently consists of two major combustion systems: a vertical, downfired salt type unit with complete wet quench system, and a three-stage, low NOx horizontal denoxidizer system. Both units are designed to be easily reconfigured to allow numerous process configurations. The computer control system and its leading edge data acquisition system also enhance the capabilities of the test facility. A separate pad, complete with stack, utility hook-ups, and flue gas sampling, is also available for checkout and specialty combustion testing for our customers. Our R&D facility investment and capabilities, along with our dedication to quality and continually improving training options, underscore our commitment to being the leader in the worldwide environmental and combustion industry. Reducing furnace at our research facility Downfired oxidizer in Honeywell UOP Callidus research facility

Honeywell UOP Callidus headquarters - Tulsa, Oklahoma. USA Honeywell UOP Callidus combustion test facility - China Honeywell UOP Callidus 82,000 sq. ft. manufacturing and fabrication facility in USA Global Coverage Honeywell UOP Callidus reaches the global market through our headquarters located in Tulsa, Oklahoma, USA, with regional direct sales offices and independent sales representation around the world. Meeting our customers expectations and setting the standards for the combustion industry have always been our goals. Each, flare, thermal oxidizer and catalyst system we design and manufacture is built with those goals in mind. Test Facility Honeywell UOP Callidus test facilities in the U.S. and China are used for combustion technology research and development, as well as for customer demonstrations. Our array of test systems allow us to closely match actual field conditions, providing results that will more accurately predict actual measured performance. In Addition to Oxidizer Systems, Honeywell UOP Callidus Offers: Ultra-low NO x s Flares, flare systems and flare gas recovery systems Thermal oxidizer systems Field services and parts CFD Modeling Training and schools ISO 9001:2008 Certification High-Performance Combustion Solutions Service Parts Installation Contact us we re here to help. CallidusHelp@Honeywell.com USA Certification China Certification For more information For more information, please visit www.callidus.com to find a local sales representative Corporate Headquarters Callidus Technologies 7130 South Lewis Ave. Suite 335 Tulsa, Oklahoma. 74136 Tel: +1-918-496-7599 www.callidus.com UOP7326-7 March 2016 Printed in U.S.A. 2016 UOP LLC. All rights reserved.