SAVECO
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SAVECO
SAVECO SaveTechnology Technology & & Engineering Engineering Save Introduction to Products and Services Design & Manufacture Dusty Air Treatment Work Environment Improvement Waste Water Treatment Flue Gas Treatment Research & Developement SAVECO Save & Engineering SaveTechnology Technology & Engineering Design & Manufacture of Pollution Control Device for Clean Your Workplace SAVECOⓡ Dusty Air Treatment DESIGN of Air Pollution Control Device Developing an optimized air pollution control system requires the consideration of a wide range of engineering, environmental, economic,and regulatory factors. At SAVECO, we have assisted a wide variety of industrial, municipal, and research clients with the selection and design of effective air pollution control systems. Raw Material Pollutant Emissions Particulate Matter : TSP, PM10, PM2.5 Gaseous Materials : SOx, NOx, VOCs, Odor Products SAVECO 는 발생원의 확인, 설계를 통한 필요 용량 산정, 산업안전보건법과 환경법의 검토, 대기오염 방지시설 설계, 시공 및 인허가에 이르기 까지 고객의 입장에서 프로젝트를 수행합니다. Hazardous Single Particle in Workplace Air Pollution Control System Design Factor Characteristics of Pollutants and Source Emission Amounts and Treatment Polluted Air Volume Cost and Benefit Geometric Conditions Criteria of Environmental Law SAVECOⓡ Dusty Air Treatment CYLOBER SYSTEM Principle Dust and Gas Treatment Device Design Installation SCRUBBER SYSTEM Hazardous and Odor Gas Treatment Device Principle Design SAVECOⓡ Dusty Air Treatment BAG HOUSE SYSTEM Principle Dust Collect Device by Filtration Design Manufacture Sanding SA1-1/2 Coating Urethane >160㎛ Packing & Delivery SAVECOⓡ Dusty Air Treatment ADSORPTION TOWER Odor & VOCs Removal Device by Activated Carbon The SAVECO Activated Carbon Adsorbers are well suited for the removal of VOC’s from high flow air streams and other emission control applications. Some typical applications for the SAVECO Adsorbers include: • Industrial plant emissions • Soil vapor extraction (SVE) remediation system off-gases • VOC removal from dusty air emissions • Backup VOC control device for thermal oxidizers. The frequency of adsorber exchange will depend on operating parameters that affect carbon loading such as VOC type and concentration, temperature, relative humidity, superficial gas velocity, carbon type (coconut shell or coal) and other factors. Carbon Adsorber Body Casing Carbon Adsorber Installation(200CMM), PL Carbon Adsorber(600CMM), Mlawa, PL SAVECOⓡ Work Environment Improvement DESIGN of Workplace Ventilation System SAVECO, our proven industry experience in industrial ventilation means we can help you maximize system effectiveness and reliability. We offer industrial ventilation service to investigate the existing air pollution control systems at your facility and to provide technical recommendations as well as conceptual design necessary to attain the desired indoor and outdoor air quality. SAVECOⓡ Waste Water WasteTreatment Water Treatment System Water Treatment Process SAVECO Has established an outstanding waste water treatment system. At SAVECO, Wastewater treatment system is a combination of physical and biological process designed to remove organic matter from wastes. Heavy Metal Waste Water Treatment System SAVECO Has established an heavy metal waste water treatment system that both effectively and economically removes heavy metals from these types of waste water. Applications ● Metal Process Plant ● Metal surface treatment Plants ● Waste water from dyeing plants ● Food Processing Plant ● Mining Waste Water SAVECOⓡ Flue Gaseous Treatment Process Flue Gaseous Treatment Bag House Stack SDR or SNCR Cyclone or Scrubber Boiler Fan Heat Exchanger The hot flue gasses pass from the incinerator ① to the gas cooler ② via either an underground canal or overhead flue duct. The gas cooler ② comprises two water cooling circuits, and one combustion air pre heat section which improves the incinerator efficiency. The water cooling circuits are connected to a back cooler ③ which is mounted outdoors. he cooled gasses then pass through a cyclone separator ④ which removes all but the finest dust particles from the gas stream. Separated dust leaves via a cell wheel sluice and falls into the collecting bin ⑤. The gasses then pass to the ball rotor recycling and conditioning unit ⑥. A the start of each working day, a pre determined quantity of fresh adsorbent is automatically loaded from its storage container ⑦. The gas stream passing through the ball rotor unit will be treated by the adsorbent, some of which will be entrained in the gas stream leaving this section. It then passes into the SDR/SNCR ⑧, where hazardous gas plus the entrained adsorbent will be removed. An automatic system cleans the bags by inflating them in order to dislodge the accumulated deposits. These deposits fall to the bottom of the unit ⑨, where the majority is returned to the ball rotor unit. This ensures that the adsorbent is recycled until it is fully used. Any rejected deposits are removed through a cell wheel and fall into a collection bin ⑩. The completely clean gasses pass from the bag filter through the induced draught fan ⑪ to the exhaust stack. SAVECOⓡ Research & Development Research Emission Characteristics From Source Materials Research Objectives Coating materials are composed of very complex chemical compounds, these indoor building materials discharge very much VOCs. We performed the environmental chamber test to investigate the TVOCs emission characteristics and emission factor about paints. As the result, we knew that those of TVOCs emission characteristics are high emissions at initial time and decreased in course of time. The emission factor-time profile showed good fit with the results from the measured and predicted value SAVECOⓡ Research & Development Development Liquid-Composting System [Mass conversion of NH4] Raw materials • pH : 7.6 • NH4-N : 5,378 mg/L pH adjustment Ammonia stripping • pH : 10.9 • Ca(OH)2 : 48 g/L • NH4-N : 4,673 mg/L • pH : 10.9 • Air flow : 30 lpm • Temp : 25 ℃ • Volume : 10 L Ammonia Recovery : 68.4 % Ammonia Removal : 82.3 % Stripped manure • NH4-N : 1,081 mg/L • Volume : 8.8 L Absorbent • NH4-N :8,651 mg/L • Volume : 3.5 L Schematic view of aerobic liquid composting system: ①Blower, ②Exhaust fan, ③pH Sensor #1, ④Flow control pump #1, ⑤Spray pump, ⑥Temperature sensor, ⑦Circulation pump #1, ⑧Circulation pump #2, ⑨pH sensor #2, ⑩DO sensor, ⑪Flow control pump #2, ⑫Oxygen tank, ⑬Chemical feeder #1, ⑭Chemical feeder #2, ⑮Chemical tank #1, ⑯Chemical tank #2, ⑰Oxygen injector #1, ⑱Oxygen injector #2, ⑲Regulator PILOT TEST – LIQUID COMPOSTING rd Step 2 Aerobic Reaction 3 nd 1. Air Supply DO : 1.0 ~ 2 ppm 2. Retention Time : 4 days 3. Reaction Temp. 25~35 ℃ Items Raw After 7d Tempereature Aerobic test I Aerobic test II Raw After 7d 40 35 30 pH 7.1 7.6 7.8 7.6 25 Sample Temp., ℃ 27 32 26 31 20 Amb. Temp., ℃ 24 24 26 26 Ambient RH, % 79 75 74 73 6,502 1,806 5,993 2,217 -1 T-N, mg L NH3-N, mg L-1 5,378 1,712 4,549 2,132 -1 1,121 91 16.8 14.7 4.7 12.3 3.4 8.1 VS, % 3.6 8.7 2.1 6.2 FS, % 1.1 3.6 1.3 1.9 NO3-N, mg L TS, % Water content, % 95.3 87.7 96.6 5.2 6.8 8.5 12 91.9 0 2 4 6 8 10 12 Time (day) 40 12 11 30 10 20 9 pH 2nd Step 1st Aerobic Reaction 1. pH : 7.6 ~ 7.4 2. Microbial Feeding 3.Oxygen Supply DO : 3 ~ 5 ppm 4. Retention Time : 3 days 5. Reaction Temp. : 35~45 ℃ Summary on major components of liquid compost Temperature Operation Condition & Procedure 1. Raw Material Supply 2. pH : 9.5~10.5 3. Air supply - air stripping 1st Step 4. Temp. Range Pre-Treatment Temp. : 20 ~ 25 ℃ 5. Air/Liquid ratio : 1 m3/m3-min 6. Retention Time : 48hrs 50 45 8 10 7 Temp. pH 0 6 0 50 100 150 200 250 300 Time (hr) Liquid manure can be successfully composted by our aerobic-liquid composting methods. The liquid composting manure maintained high temperature over the initial reaction period, about 3 days. The curing compost continued to stay hot for an expended period of time, beyond the typical seven to fifty days. Aerobic composting of liquid manure to produce organic fertilizer results in a significant reduction in C/N ratio from livestock operations, compared to the raw materials. Most of the reduction in mass (water content, carbon) occurs during the active aerobic composting phase while organic component in total nitrogen and suspended particulate were increased. SAVECOⓡ Established in 2004 Creator of Environment Engineering and Technology SAVECO Save Technology & Engineering Tel) 032-326-4264,5 www.saveco.co.kr Fax) 032-326-4266 Water Air Source Control Emission Control Emission Control Pollutants Removal Total Environmental Solutions Waste Waste Treatment Workplace Improvement of poor workplace