Search results for: 'Production capa''

REFERENCE NUMBER: YY-1365 CONTINUOUS PRODUCTION LINE FOR IMPREGNATION, DRYING, ABRASIVE SPRAY, HEAT-SETTING OF SYNTHETIC FIBERS FOR ABRASIVE WADDINGS, WITH AIRLAY CARDING MACHINE AND FIBER PREPARATION DETAILS: MAIN FEATURES: - THREE LAYERS OVEN: TWO UPPER DRYING LAYERS WITH LENGTH OF 6+ 6 METERS; ONE LOWER CURING LAYER WITH A LENGTH OF 6 METERS; - HEATING: BY DIRECT HEATING WITH AUTOMATIC BURNERS; - CONVEYOR WIDTH: 2200mm; - WORKING WIDTH: 2000mm; - MAX DRYING AND POLYMERISATION TEMPERATURE: 230°C; - HEATING POWER: 4 BURNERS 350 KW EACH ONE, ABOUT TOTAL 1.400 KW; - VENTILATION: SEMI-CLOSED SYSTEM WITH 4 CENTRIFUGAL VENTILATORS; - ADJUSTABLE CONVEYOR SPEED BY A.C. MOTORS; - INSTALLED ELECTRIC POWER: 200 KW. APPROX.; - MECHANICAL SPEED: 2÷15 METERS PER MINUTE; - CONVEYOR DRIVING: BY A.C. MOTORS; - MANUFACTURED ARTICLE: SYNTHETIC FIBERS ABRASIVE WADDING. Learn More

T-8404 AUTOMATIC MATTRESS HOTMELT GLUE LINE CONTENT OF LINE HOT MELT SITATION UNIT - WITH HOT MELT UNIT (CORNER AND CENTER GLUING) TRANSPORTATION CONVEYOR WITH ANTISTATIC SILICON BELT (2 SETS) MATTRESS FLIPPING CONVEYOR (1 SET) AUTOMATIC PRESSING SYSTEM (1 SET) Learn More

J-3689 LAMINATION LINE, WORKING WIDTH 2200mm, YEAR 2003 & 2005 COMPOSED OF: MEYER PST-2300 POWDER SCATTERING UNIT WORKING WIDTH 2200mm YEAR: 2005 QUANTITY: 1 SCHAETTI KANNEGIESSER TLM-V LAMINATION MACHINE OVEN IS ELECTRICALLY HEATED WORKING WIDTH : 2000mm FLATBED YEAR : 2003 RHOSS MODEL CWA/EX COOLER Learn More

REFERENCE NUMBER: T-6985 COGENERATION PLANT 1.2 MEGAWATTS NEAR NEW COGENERATION SYSTEM WITH MODULAR DESIGN THAT HAS NEVER BEEN RUN IN PRODUCTION: THIS SYSTEM IS A 1.2-MEGAWATT POWER PLANT AND CAN BURN BARK, SAWDUST, AGRICULTURAL WASTES SUCH AS PEANUT SHELLS, RICE HULLS, STRAW, ANIMAL RESIDUE, WET WOOD, ETC. THIS SYSTEM WILL CONVERT SUCH WASTE PRODUCTS INTO USEABLE THERMAL AND ELECTRICAL ENERGY. THIS SOLID WASTE STREAM CAN BE CONVERTED INTO PARTICLE FORM BY THE USE OF A COMMERCIAL SHREDDER, CONVEYED TO A SILO FOR STORAGE, AND THEN FED AUTOMATICALLY INTO THE MULTI-ZONE BURNER. STEAM IS GENERATED THROUGH A LOW PRESSURE 275 DEGREE (DE-RATED FROM 300 DEGREE) STAINLESS STEEL BOILER WITH A HEAT EXCHANGER. INLET STEAM IS 475 PSIG AT 700 DEGREES FTT WITH A MAXIMUM OF 22,000 LBS/HOUR BUT COULD BE INCREASED TO 24,000 LBS/HOUR. EXHAUST STEAM PRESSURE IS 3" HGA AT 5449 RPM BUT DESIGNED TO RUN AT 4" ABSOLUTE VACUUM. STEAM IS TRANSFERRED TO THE 3-STAGE BACK PRESSURE TURBINE RATED AT 1654HP DETUNED TO 1200HP TO MATCH THE GENERATOR. THIS SYSTEM COMES COMPLETE WITH GENERATOR CONTROL CENTER, BOILER CONTROL CENTER, COMBUSTION CONTROL CENTER, CONTROL ROOM SWITCHBOARD, TURBINE OIL SYSTEM, DUST DELIVERY CONTROL SYSTEM, SWITCHGEAR AND PLC CONTROLS. THIS PLANT WAS NEW IN 2005/2006 WHEN INSTALLED AND HAS NEVER BEEN RUN EXCEPT FOR PERMITTING FUNCTION. THE TURBINE GEARBOX AND GENERATOR WERE OEM REBUILT. THE COMPANY PURCHASED THIS SYSTEM WITH A GUARANTEE THE BURNER COULD MEET NOX STANDARDS. AFTER INSTALLATION, THE BURNER COULD NOT EFFICIENTLY BURN FIBER WITH HIGH FORMALDEHYDE CONTENT. CONSEQUENTLY, THE BURNER COULD NOT MEET THOSE NOX STANDARDS THAT ARE ONE OF THE MOST STRINGENT SET OF STANDARDS IN NORTH AMERICA. THESE MULTI-STAGE BURNERS ARE USED THROUGHOUT NORTH AMERICA AND MEET OR EXCEED NOX CONTROL STANDARDS IN OTHER AREAS WITHOUT PROBLEMS. THIS COGEN SYSTEM CAN BE PROFESSIONALLY DISMANTLED, ALL EQUIPMENT TAGGED FOR REINSTALLATION AND SHIPPED TO YOUR FACILITY, REASSEMBLED, AND CONNECTED TO YOUR PRESENT ELECTRICAL GRID SYSTEM. IT WOULD TAKE APPROXIMATELY 10 WEEKS TO DISMANTLE THE PLANT AND 15 TRUCKS TO SHIP THE EQUIPMENT TO YOUR PLANT SITE, AND APPROXIMATELY 16 WEEKS TO REASSEMBLE. THIS PLANT WOULD INCLUDE EVERYTHING NEEDED EXCEPT FUEL PROCESSING (GRINDING), STORAGE AND A TRANSFORMER TO SUPPLY POWER TO YOUR FACILITY. SHIPMENT OF THE PLANT WOULD BE BROKEN DOWN AS FOLLOWS: FIVE 53' TRAILER VANS TO LEGAL WEIGHT TEN 53' FLATBED TRAILERS TOTAL WEIGHT OF COGEN PLANT EQUIPMENT = 581,000 LBS. TIE-DOWN GEAR, CHAINS, BLOCKS AND CHOKES = 6,000 LBS. GROSS CUBIC SETTING OF CARGO = 67,840 CUBIC FEET MACHINERY PROPOSAL USED 1.2-MEGAWATT POWER PLANT CONSISTING OF THE FOLLOWING: DESCRIPTION OF EQUIPMENT 3-STAGE BURNER BOILER EGR FAN ID FAN SUPPLY WATER TANK SERVICE WATER PUMP WATER SOFTNER AND FILTER BOILER WATER PUMP SYSTEM DUAL CYCLONE SEPARATOR ELECTROSTATIC PRECIPITATOR ESP TRANSFORMER ESP PUMP SYSTEM CONDENSER PUMP SYSTEM STEAM TURBINE SENTINEL GENERATOR GENERATOR CONTROL CENTER BOILER CONTROL CENTER COMBUSTION CONTOL CENTER PLANT #2 SWITCHGEAR CONTROL ROOM SWITCHBOARD TURBINE OIL SYSTEM DUST DELIVERY CONTROL SYSTEM CONDENSER CONTROL PANEL ESP CONTROL PANEL TURBINE OIL CONTROL PLANT #1 POWER SWITCHGEAR COGENERATION PROJECT LOADING ANALYSIS BOILER FEEDWATER TANK LOADPOINT: LP4 FOOTING LENGTH 9.00 FT WIDTH 9.00 FT DEPTH 0.67 FT COUNT 1 EA CUBIC FT 54.03 CUFT TOTAL CU FT 54.03 CUFT LOAD CENT. HT. 4.00 FT MACHINE FOOT: LENGTH 6.00 FT WIDTH 6.00 FT COUNT 1.00 EA TYPE 1 MACHINE WT. 16,000 LBS FOOTING WT. 8,104 LBS FOOTING LOAD 197.53 LBS/SQFT SOIL LOADING 297.58 LBS/SQFT *TANK ASSEMBLY IS BOLTED DOWN 1=EVENLY DISTRIBUTED ACROSS BASE 2=CONCENTRATED FOOTPRINT APPROX. PSF WHICH IS DISTRIBUTED OVER ENTIRE SLAB COGENERATION PROJECT LOADING ANALYSIS STEAM UNIT LOADPOINT: LP3 - FOOTING LENGTH 25.00 FT - 13.00 FT WIDTH 14.00 FT - 3.00 FT DEPTH 1.00 FT - 2.00 FT COUNT 1 EA - 3 EA CUBIC FT 350.00 CUFT - 234.00 CUFT TOTAL CU FT 584.00 CUFT LOAD CENT. HT. 8.00 FT MACHINE FOOT: LENGTH 10.30 FT WIDTH 1.00 FT COUNT 3.00 EA TYPE 2 MACHINE WT. 53,000 LBS FOOTING WT. 52,500 LBS FOOTING LOAD 151.43 LBS/SQFT SOIL LOADING 301.43 LBS/SQFT *BOILER ASSEMBLY IS BOLTED DOWN 1=EVENLY DISTRIBUTED ACROSS BASE 2=CONCENTRATED FOOTPRINT APPROX. 1,715.21 PSF WHICH IS DISTRIBUTED OVER ENTIRE SLAB COGENERATION PROJECT LOADING ANALYSIS CONDENSOR UNIT LOADPOINT: LP2 FOOTING LENGTH 23.00 FT WIDTH 3.00 FT DEPTH 3.00 FT COUNT 6 EA CUBIC FT 1,242.00 CUFT TOTAL CU FT LOAD CENT. HT. NA* FT MACHINE FOOT: LENGTH 2.00 FT WIDTH 2.00 FT COUNT 6.00 EA TYPE 2 MACHINE WT. 40,000 LBS FOOTING WT. 186,300 LBS FOOTING LOAD 1,666.67 LBS/SQFT SOIL LOADING 546.62 LBS/SQFT *CONDENSOR ASSEMBLY IS WELDED DOWN 1=EVENLY DISTRIBUTED ACROSS BASE 2=BASE PAD LOADING IS CONDCENTATED COGENERATION PROJECT LOADING ANALYSIS TURBINE-GENERATOR SET LOADPOINT: LP6 FOOTING LENGTH 21.00 FT WIDTH 9.00 FT DEPTH 1.00 FT COUNT 1 EA CUBIC FT 189.00 CUFT TOTAL CU FT 189.00 CUFT LOAD CENT. HT. 3.50 FT MACHINE FOOT: LENGTH 6.00 FT WIDTH 6.00 FT COUNT 1.00 EA TYPE 1 MACHINE WT. 38,000 LBS FOOTING WT. 28,350 LBS FOOTING LOAD 201.06 LBS/SQFT SOIL LOADING 351.06 LBS/SQFT * ASSEMBLY IS BOLTED DOWN 1=EVENLY DISTRIBUTED ACROSS BASE 2=CONCENTRATED FOOTPRINT APPROX. NA PSF WHICH IS DISTRIBUTED OVER ENTIRE SLAB COGENERATION PROJECT LOADING ANALYSIS COMBUSTION UNIT LOADPOINT: LP1 LENGTH 24.75 FT WIDTH 8.50 FT DEPTH 1.00 FT COUNT 1 EA CUBIC FT 210.38 CUFT TOTAL CU FT LOAD CENT. HT. 6.50 FT MACHINE FOOT: LENGTH 24.58 FT WIDTH 7.60 FT COUNT 1.00 EA TYPE 1 MACHINE WT. 80,000 LBS FOOTING WT. 31,556 LBS FOOTING LOAD 428.25 LBS/SQFT SOIL LOADING 597.17 LBS/SQFT *BURNER ASSEMBLY IS BOLTED DOWN 1=EVENLY DISTRIBUTED ACROSS BASE COGENERATION PROJECT LOADING ANALYSIS WET ESP UNIT LOADPOINT: LP5 FOOTING LENGTH 9.00 FT WIDTH 9.00 FT DEPTH 0.67 FT COUNT 1 EA CUBIC FT 54.03 CUFT TOTAL CU FT 54.03 CUFT LOAD CENT. HT. 9.00 FT MACHINE FOOT: LENGTH 6.00 FT WIDTH 6.00 FT COUNT 1.00 EA TYPE 1 MACHINE WT. 38,000 LBS FOOTING WT. 8,104 LBS FOOTING LOAD 469.14 LBS/SQFT SOIL LOADING 569.19 LBS/SQFT * ASSEMBLY IS BOLTED DOWN 1=EVENLY DISTRIBUTED ACROSS BASE 2=CONCENTRATED FOOTPRINT APPROX. NA PSF WHICH IS DISTRIBUTED OVER ENTIRE SLAB COGENERATION CONCRETE FOOTING LOADING ANALYSIS LIVE + LOAD DEAD FOOT WIND THICKNESS YDS WIEGHT POINT DESCRIPTION WEIGHT LENGTH WIDTH QTY PSF LOAD LBS INCHES LBS 1 COMBUSTION UNIT 80,000 25 8 1 400 12 7.41 2 CONDENSER STRUCTURE 80,000 3 3 6 1,481 36 6.00 3 STEAM GENERATOR 105,500 3 12 3 977 12 4.00 4 BOILER FEED WATER TANK 16,000 9 9 1 198 4 1.00 5 WESP UNIT 38,000 8 8 1 594 12 2.37 6 TURBINE GEN SET 32,000 6 23 1 232 12 5.11 7 SILO* 230,000 21 21 1 345,000 36 49.00 330,750 PAVE UNDER STEAM UNIT 12 28 1 4 4.15 MISC. STEEL FOOTINGS 1.5 1.5 15 12 1.25 MISC AREA PAVEMENT 72 5 1 4 4.44 84.73 8.47 FACTOR ESTIMATED CONCRETE USAGE 93.20 YARDS * SPECIFICATION MIGHT CHANGE WHEN ENGINEERING DRAWINGS COME FROM MANUFACTURER FUEL METERING BIN FUEL IS TRANSFERRED FROM A STORAGE BIN TO THE METERING BIN. THE METERING BIN IS PROVIDED TO PLACE A SUPPLY OF FUEL IN CLOSE PROXIMITY TO THE COMBUSTION SYSTEM AND ASSURE A CONSTANT SUPPLY OF FUEL TO THE COMBUSTION SYSTEM. THIS IS USUALLY A SMALL BIN PROVIDING UP TO TWO HOURS OF FUEL STORAGE CLOSE TO THE COMBUSTION SYSTEM. BIN IS SUPPLIED WITH A HATCH AND A SIGHT GLASS FOR EASILY DETERMINING THE QUANTITY OF FUEL PRESENT. THE METERING BIN IS EQUIPPED WITH A LIVE BOTTOM AUGER SYSTEM TO ASSURE A CONSTANT FLOW OF FUEL TO THE COMBUSTION SYSTEM. THE FUEL FLOWS INTO A SCREW CONVEYOR THAT TRANSPORTS THE FUEL TO THE COMBUSTION SYSTEM. THIS BIN IS EQUIPPED WITH HIGH- AND LOW-LEVEL SENSORS. FAILURE OF THE FUEL TRANSFER CONVEYORS OR A PROBLEM WITH THE PRIMARY FUEL STORAGE DEVICES IS SIGNALED WHEN THE METERING BIN LEVEL IS LOW FOR AN ADJUSTABLE PERIOD OF TIME. THE DRIVE MOTOR AND LEVEL SWITCHES ARE WIRED TO A JUNCTION BOX ON THE METERING BIN. METERING BIN SIZES WILL VARY ACCORDING TO THE FUEL NEEDS OF THE COMBUSTION SYSTEM. THESE BINS ARE SUPPLIED WITH OPEN TOPS WHEN THE CUSTOMER IS RESPONSIBLE FOR DELIVERY OF FUEL TO THE METERING BIN. THESE BINS WILL USUALLY BE ELEVATED ABOVE THE COMBUSTION UNIT FEED SCREW CONVEYOR. LEGS CAN BE PROVIDED WITH THESE UNITS TO SUPPORT THE METERING BINS FROM THE FLOOR OR THE CUSTOMER CAN PROVIDE SUPPORTS AS APPROPRIATE. THE UNITS ARE SUPPORTED FROM BELOW AT THE FOUR CORNERS OF THE BIN. COMBUSTION SYSTEM THE COMBUSTION SYSTEM CONSISTS OF SEVERAL COMPONENTS AS FOLLOWS: 1. FUEL FEED ROTARY AIR LOCK 2. FUEL FEED TRANSITION HOPPER AND HIGH/LOW LEVEL SENSORS 3. FUEL FEED SCREW CONVEYOR, EQUIPPED WITH VARIABLE FREQUENCY DRIVE 4. PRIMARY COMBUSTION CHAMBER, CONTAINING: A. CERAMIC WALL AND ARCH SYSTEM B. THREE LEVEL COMBUSTION AIR INLETS WITH INDIVIDUAL ADJUSTMENTS AND COMBUSTION AIR FANS. COMBUSTION AIR FANS ARE EQUIPPED WITH VARIABLE FREQUENCY DRIVES C. STATIONARY GRATE SYSTEM FOR INTRODUCTION OF PRIMARY AND SECONDARY COMBUSTION AIR D. ASH AUGER SCREWS FABRICATED OF HIGH TEMPERATURE STAINLESS STEEL FOR ASSURING PROPER DISTRIBUTION OF THE FIRE WITHIN THE FIRE BOX AND AUTOMATIC REMOVAL OF THE ASH REMAINING FROM THE COMBUSTION OF THE FUEL MATERIAL. 1. SECONDARY COMBUSTION CHAMBER A. CERAMIC WALL AND ARCH SYSTEM B. PROVIDES FOR AN EXTENDED DWELL TIME TO ASSURE COMPLETE COMBUSTION OF THE COMBUSTION BYPRODUCT GASES PRIOR TO LEAVING THE COMBUSTION SYSTEM. 1. HOT GAS TRANSITION FOR COMBUSTION UNIT TO HEAT EXCHANGER UNIT 2. HOT GAS DUCT WORK FROM HEAT EXCHANGER TO THE DUST COLLECTION EQUIPMENT 3. DUST COLLECTION EQUIPMENT, DESIGN DEPENDING ON FUEL AND SYSTEM SIZE 4. DUCT WORK FROM DUST COLLECTION EQUIPMENT TO INDUCED DRAFT FAN 5. INDUCED DRAFT FAN, EQUIPPED WITH VARIABLE FREQUENCY DRIVE OR AUTOMATICALLY ADJUSTABLE DAMPER, DEPENDING ON SYSTEM DESIGN AND APPLICATION. 6. EXHAUST GAS STACK, DIAMETER AND HEIGHT DEPENDING ON SYSTEM DESIGN AND APPLICATION. THE COMBUSTION SYSTEM IS PREFABRICATED TO THE EXTENT THAT IS ALLOWABLE FOR NECESSARY SHIPPING RESTRICTIONS. IN GENERAL, THE PRIMARY COMBUSTION CHAMBER IS COMPLETELY PREFABRICATED IN THE SHOP. COMBUSTION AIR FANS AND MANIFOLDS ARE INSTALLED ON THE JOB SITE. THE SIZES OF THE COMBUSTION SYSTEMS FOR THE 600 SERIES ARE APPROXIMATELY 8 FEET WIDE. THE LENGTH OF THE UNITS IS APPROXIMATELY 25 FEET. THE OVERALL HEIGHT OF THE UNIT IS APPROXIMATELY 8 FEET. THE PRIMARY COMBUSTION CHAMBERS ARE SHIPPED COMPLETE. THE EXTENDED COMBUSTION CHAMBERS ARE SHIPPED AS COMPONENTS. STEAM BOILER SYSTEMS THE STEAM BOILER SYSTEM CONSIST OF THE NEEDED EQUIPMENT ITEMS TO PRODUCE STEAM ENERGY FROM THE HOT GASES PRODUCED BY THE CHALLENGER COMBUSTION SYSTEMS. THE BOILER IS A 300PSIG, 18,819 LBS. PER HOUR. THIS SYSTEM IS MADE UP OF THE FOLLOWING COMPONENTS: HEAT RECOVERY STEAM GENERATOR (HRSG) BOILER FEEDWATER PUMP SKID BOILER FEEDWATER STORAGE VESSEL FEEDWATER TREATMENT SKID THE HRSG UNITS ARE SIZED TO RECOVER APPROXIMATELY 75 80% OF THE THERMAL ENERGY ENTERING THE DEVICE. THE STEAM ENERGY OUTPUT IS DETERMINED BY ESTABLISHING THE THERMAL ENERGY RELEASED BY THE COMBUSTION SYSTEM TO THE HOT GASES THAT WILL BE ENTERING THE HRSG. THE STEAM FLOW OUTPUT IS DETERMINED BY ESTABLISHING THE DESIRED STEAM PRESSURE AND THE HEAT INPUT. STEAM PRODUCTION WILL VARY ACCORDING TO THE QUANTITY AND TEMPERATURE OF THE HOT GASES PRODUCED IN THE COMBUSTION SYSTEM AND THE TEMPERATURE OF THE BOILER FEEDWATER AS WELL AS THE STEAM PRESSURE DESIRED. SYSTEM INCLUDES: ECONOMIZER - INSTALLED IN OUTLET OF HRSG CONDENSATE HEATER - STEAM OPERATED - INSTALLED IN THE BOILER FEEDWATER STORAGE VESSEL SOOT BLOWER - INSTALLED IN THE HRSG TO MINIMIZE THE EFFECTS OF ASH CARRY DEAERATOR - INSTALLED IN THE BOILER FEEDWATER STORAGE VESSEL THIS HEAT RECOVERY STEAM GENERATOR UNIT WAS DESIGNED AS A FIRE TUBE BOILER FOR A SINGLE PASS OF THE HOT GASES THROUGH THE UNIT WITH STEAM PRESSURES UP TO 300 PSIG. THE UNIT WAS DESIGNED WITH AMPLE STEAMING VOLUME TO ASSURE A GOOD QUALITY OF STEAM GENERATION. STEAM IS OF A QUALITY SUFFICIENT TO ENTER INTO A STEAM TURBINE GENERATOR UNIT. BOILER FEEDWATER PUMP PACKAGE IN ADDITION TO THE BOILER, A BOILER FEED WATER PUMP PACKAGE IS INCLUDED. THIS PACKAGE CONSISTS OF A PREFABRICATED SKID CONTAINING TWO BOILER FEEDWATER PUMPS AND NECESSARY PIPING AND VALVES. ONE PUMP IS THE DESIGNATED “RUN” PUMP AND THE OTHER IS A DESIGNATED “SPARE” PUMP. A FLOW METER, PRESSURE GAUGES AND TEMPERATURE GAUGE ARE PROVIDED FOR MONITORING THE PERFORMANCE OF THE PACKAGE. PUMPS ARE SIZED FOR 125% OF DESIGN CAPACITY AND ARE INTENDED TO RUN CONTINUOUSLY TO MAINTAIN DESIRED BOILER DRUM LEVEL. PUMP PACKAGES ARE SIZED TO MATCH THE HEAT RECOVERY STEAM GENERATOR UNITS. BOILER FEEDWATER STORAGE TANK THE SYSTEM ALSO INCLUDES A BOILER FEED WATER STORAGE TANK. THIS PACKAGE CONSISTS OF AN INSULATED TANK FOR STORAGE OF CONDENSATE AND BOILER FEEDWATER FOR THE BOILER SYSTEM. THE TANK IS CONSTRUCTED TO A 15 PSIG RATING AND CAN BE OPERATED AT A PRESSURE OF 5 PSIG IF NECESSARY. STANDARD DESIGNS CALL FOR VENTED TANKS. A FLOW METER FOR CONDENSATE RETURN AND A FLOW METER FOR MAKEUP WATER ARE PROVIDED. A PRESSURE GAUGE, LEVEL GAUGE AND TEMPERATURE GAUGE ARE PROVIDED FOR MONITORING THE CONDITION OF THE CONDENSATE WITHIN THE TANK. THE TANK IS PROVIDED WITH A STAND TO ELEVATE THE TANK ABOVE THE SUCTION OF THE BOILER FEEDWATER PUMPS. IN SOME CASES, IT WILL BE DESIRABLE TO LOCATE THE TANK ABOVE THE INLET TO THE BOILER. THE STANDS FOR THESE APPLICATIONS ARE TO BE PROVIDED BY THE CUSTOMER. THE TANK IS SIZED TO PROVIDE FOR OPERATION OF THE BOILER AT FULL OUTPUT FOR A PERIOD OF UP TO 20 MINUTES. THE TANK IS ALSO EQUIPPED WITH INSTRUMENTATION TO TIE THE UNIT INTO THE OVERALL COMBUSTION/BOILER CONTROL SYSTEM. THE FOLLOWING DEVICES/INPUTS ARE PROVIDED: TEMPERATURE SENSOR, PRESSURE SENSOR, LEVEL SENSOR, AND FIVE POINT LEVEL SWITCH FOR ALARMS AND SHUTDOWN LOGIC. THE PACKAGE IS ALSO EQUIPPED WITH AN AUTOMATIC WATER VALVE TO PROVIDE MAKEUP WATER IN THE EVENT THE WATER LEVEL REACHES THE LOW-LEVEL ALARM POSITION. THIS IS PROVIDED THROUGH A FLOAT OPERATED VALVE. THE TANK AND CONTROL DEVICES ARE PRE-PACKAGED WITH ALL CONTROL DEVICES WIRED TO A JUNCTION BOX MOUNTED ON THE UNIT. THE OPERATING VOLTAGE FOR THE CONTROL DEVICES IS 24VDC. THE TANK IS ALSO INSULATED TO REDUCE HEAT LOSS TO THE ATMOSPHERE. DEAERATORS A DEAERATOR HAS BEEN PROVIDED TO REMOVE UNWANTED OXYGEN AND OTHER NON-CONDENSABLE GASES FROM THE BOILER FEEDWATER. THE DEAERATOR IS PROVIDED FOR THIS PURPOSE. THIS IS GENERALLY A REQUIRED ITEM ON 150 AND 300 PSIG STEAM SYSTEMS. THIS IS A REQUIRED DEVICE ON ALL STEAM SYSTEMS PROVIDING STEAM FOR STEAM TURBINE GENERATOR APPLICATIONS. FEEDWATER TREATMENT PACKAGES BOILER FEED WATER MUST BE OF HIGH QUALITY, ALL CONTAMINANTS THAT WOULD DAMAGE THE BOILER OR STEAM TURBINES MUST BE REMOVED FROM THE FEED WATER STREAM. THERE ARE GENERALLY THREE AREAS OF CONCERN. FIRST, THE WATER MUST BE FREE FROM SOLIDS SUCH AS SAND OR OTHER CONTAMINANTS. SECOND, DISSOLVED MINERALS SUCH SODIUM AND POTASSIUM MUST BE REMOVED. THIRD, NON-CONDENSABLE GASES SUCH AS OXYGEN AND CARBON DIOXIDE MUST BE REMOVED. THE REMOVAL OF THESE CONTAMINANTS REQUIRES A THREE STAGE REMOVAL PLAN. FIRST, ALL WATER ENTERING THE BOILER SYSTEM SHOULD BE FILTERED. SECOND, THE WATER SHOULD PASS THROUGH A WATER SOFTENER UNIT OF SOME TYPE AND THIRD, CHEMICALS WILL BE ADDED TO THE WATER TO ASSIST IN THE REMOVAL OF THE NON-CONDENSABLE GASES AND OTHER CONTAMINANTS. THE FEED WATER TREATMENT PACKAGE WILL INCLUDE THE FOLLOWING EQUIPMENT: 1. WATER FILTER - DUAL UNIT 2. WATER SOFTENER - DUAL UNIT 3. CHEMICAL FEED PUMPS (3) - SEPARATE ASSEMBLY THIS EQUIPMENT IS PREPACKAGED ON A SKID. THE CONTROLS AND PUMP MOTORS ARE PRE-WIRED TO A JUNCTION BOX ON THE PACKAGE. THE CHEMICAL ADDITIVES PUMPS ARE PACKAGED INTO A PUMP STAND. THE STAND IS DESIGNED TO BE LOCATED IN A POSITION AGAINST A WALL WHERE THE CONTAINERS FOR THE VARIOUS BOILER FEEDWATER CHEMICALS CAN BE PLACED. STEAM TURBINE GENERATOR SYSTEMS AN ELLIOT MODEL 2DYR3-MULTISTAGE TURBINE WILL BE USED FOR THE SYSTEM. IT CONSISTS OF THE FOLLOWING: 5449 RPM, INLET STEAM PRESSURE 475 PSIG, INLET STEAM TEMPERATURE 700’HGA, EXHAUST STEAM PRESSURE 3” HGA, MAXIMUM INLET STEAM TEMPERATURE 750 FTT, RATED POWER 1654 HP WITH ALL HAND VALVES OPEN. IT INCLUDES: 1. GEAR REDUCER 2. ELECTRIC GENERATOR A. INDUCTION B. SYNCHRONOUS 1. LUBRICATION SYSTEM 2. INSTRUMENTATION / CONTROLS 3. GENERATOR BREAKER THE BASIC COMPONENTS WERE ASSEMBLED INTO A SKID PACKAGE. THE PACKAGE WAS PREASSEMBLED AND SHIPPED AS A COMPLETED ASSEMBLY. THE CONTROLS AND GENERATOR BREAKER ARE PRE-ASSEMBLED AND TESTED PRIOR TO BEING SHIPPED TO THE CUSTOMER. STEAM CONDENSER SYSTEMS THE PURPOSE OF A STEAM CONDENSER SYSTEM IS TO TAKE THE STEAM THAT EXITS THE STEAM TURBINE GENERATOR UNIT AND CONDENSE IT TO WATER SO THAT IT MAY BE RETURNED TO THE BOILER FEEDWATER SYSTEM. THIS ALLOWS FOR THE CONSERVATION OF THERMAL ENERGY, WATER AND THE ASSOCIATED BOILER FEEDWATER TREATMENT CHEMICALS. A WATER-COOLED DESIGN CONDENSER HAS BEEN INCLUDED. AIR COOLED CONDENSER SYSTEMS THE AIR COOLED CONDENSER SYSTEM IS MADE UP OF FRAMES THAT CONTAIN MULTIPLE ROWS OF CARBON STEEL TUBES THAT ARE WRAPPED WITH AN ALUMINUM FIN. THIS FINNED ARRANGEMENT ALLOWS THE CARBON STEEL TUBE TO CONDUCT THERMAL ENERGY INTO THE AIR SURROUNDING THE UNIT. IN ORDER TO MAXIMIZE THE HEAT DISSIPATION, THE UNITS ARE SUPPLIED WITH FANS TO MOVE THE COOLER AMBIENT AIR PAST THE FINNED TUBES. AIR POLLUTION CONTROL EQUIPMENT A COMPLETE AIR POLLUTION CONTROL SYSTEM WITH EQUIPMENT REQUIRED FOR THIS PROJECT HAS BEEN INCLUDED, BASED ON LOCAL REQUIREMENTS. THE EQUIPMENT AVAILABLE CONSISTS OF THE FOLLOWING: 1. MULTICLONE - THESE UNITS ARE DESIGNED TO REMOVE PARTICULATE MATTER THAT IS AS SMALL AS 10 MICRONS IN SIZE. SINCE AIR EMISSIONS ARE GENERALLY BASED ON A QUANTITY OF EMISSIONS ON AN ANNUAL BASIS, THOSE QUANTITIES MUST BE ESTIMATED AND QUANTIFIED. WHERE THE EMISSIONS FROM THE MULTICLONE UNIT EXCEED THOSE QUANTITIES, THEN ADDITIONAL EQUIPMENT MUST BE USED. 2. BAG HOUSES - THESE UNITS CONSIST OF MULTIPLE HIGH TEMPERATURE RATED DUST COLLECTION BAGS. THESE BAGS CAN BE PROVIDED IN DIFFERENT TYPES AND CONFIGURATIONS AS WELL AS COATED AND UNCOATED TO ACHIEVE DIFFERING COLLECTION EFFICIENCIES. THE DESIGN OF THE BAG HOUSE SYSTEMS WILL VARY ACCORDING TO LOCAL REQUIREMENTS. 3. SCRUBBERS - THESE SYSTEMS CONSIST OF A SPRAY TOWER, WATER COLLECTION BASIN, A CIRCULATING WATER PUMP SYSTEM AND A MIST ELIMINATOR SECTION. THESE UNITS INTRODUCE A FINE SPRAY OF WATER INTO THE EXHAUST GASES. THIS FINE MIST OF WATER DROPLETS ATTRACT THE DUST PARTICLES AND THE DUST PARTICLES ARE COLLECTED ON THE FINE WATER DROPLETS. THESE WATER DROPLETS THEN FALL INTO THE COLLECTION BASIN. SOME AMOUNT OF THE SPRAY IS CARRIED UP THE TOWER, THIS WATER IS COLLECTED IN A MIST ELIMINATOR SECTION OF THE TOWER AND THE COLLECTED WATER IS CHANNELED TO THE COLLECTION BASIN. A SMALL AMOUNT OF WATER IS CONTINUOUSLY BLED FROM THE COLLECTION BASIN TO REMOVE THE COLLECTED PARTICULATE MATERIAL. THIS IS GENERALLY INTRODUCED INTO THE COMBUSTION UNIT AND REMOVED BY THE ASH COLLECTION SYSTEM THAT IS A PART OF THE COMBUSTION SYSTEM. SOME SMALL AMOUNT OF WATER IS EVAPORATED AS THE COMBUSTION GASES ARE COOLED TO APPROXIMATELY 150F. A CONTINUOUS MAKE UP WATER SUPPLY IS REQUIRED. 4. WET ELECTROSTATIC PRECIPITATORS - IN SYSTEMS REQUIRING AN ADDITIONAL LEVEL OF PARTICULATE CONTROL AN ELECTROSTATIC COLLECTION UNIT IS ADDED TO THE TOP OF THE SCRUBBER SYSTEM. THIS ELECTROSTATIC UNIT REPLACES THE MIST ELIMINATOR THAT IS PROVIDED AS A PART OF THE SCRUBBER DESCRIBED ABOVE. THIS UNIT REMOVES A HIGHER PERCENTAGE OF THE DUST/WATER PARTICLES FROM THE EXHAUST GAS STREAM. CONTROL AND POWER DISTRIBUTION CONTROLS THIS COGEN PLANT HAS FULLY INTEGRATED ALL ASPECTS OF THE COGENERATIONS FACILITIES EQUIPMENT PACKAGE INTO A SINGLE CONTROL SYSTEM. THIS IS ACCOMPLISHED USING PROGRAMMABLE LOGIC CONTROLLERS AND TOUCH SCREEN OPERATOR INTERFACE DEVICES TO CREATE A WINDOW ON THE ENTIRE SYSTEM. THIS SYSTEM WAS DESIGNED FOR A MINIMUM OF OPERATOR ATTENTION. SOFTWARE IS CONFIGURED TO PRESENT CLEAR WINDOWS INTO THE FACILITIES OPERATIONS. THIS COGENERATION SYSTEM WAS SET UP WITH DUAL OPERATOR INTERFACES TO ASSURE A VIEW OF MULTIPLE OPERATING COMPONENTS AT ALL TIMES. POWER DISTRIBUTION THE POWER DISTRIBUTION EQUIPMENT IS PROVIDED AS FOLLOWS. BUT, IN GENERAL THE FOLLOWING DESCRIPTION WILL APPLY. EACH COGENERATION SYSTEM WILL BE PROVIDED WITH A FACILITY MAIN BREAKER. THIS MAIN BREAKER WILL BE PROVIDED AT THE PRIMARY VOLTAGE OF THE GENERATOR PORTION OF THE PROJECT. IN MOST CASES THIS WILL BE 480 V, 3 PH AND 60 Hz OR 400 V, 3 PH AND 50 Hz. CUSTOMERS WILL SPECIFY THE INTERCONNECTION VOLTAGE REQUIREMENTS FOR A GIVEN APPLICATION. THIS DISCUSSION IS PRESENTED BASED ON THE NOMINAL 480 VAC SYSTEM. THIS EQUIPMENT PACKAGE IS SHIPPED IN TWO PIECES; ONE INCLUDES THE MAIN BREAKER AND THE GENERATOR BREAKER AND THE OTHER INCLUDES THE VARIOUS FACILITY BRANCH BREAKERS FOR PROVIDING POWER TO THE VARIOUS SYSTEM PANELS. THE TWO PIECES ARE JOINED TOGETHER WITH A BUS SPLICE KIT ONCE INSTALLED AT THE CUSTOMER’S FACILITY. THE POWER DISTRIBUTION SYSTEM IS DESIGNED AS A MOTOR CONTROL CENTER TO FACILITATE EASY EQUIPMENT ADDITIONS IN THE FUTURE. Learn More

REFERENCE NUMBER: T-6946 SOLAR PANEL PRODUCTION PLANT, 80 MW, YEAR 2008 SOLAR PANEL PRODUCTION PLANT 80 MW OUTPUT CAPACITY PER YEAR THIN FILM SOLAR PANELS AMAT PECVD SYSTEM MODEL "NEW ARISTO" (VERTICAL SPUTTER WITH 14 CHAMBERS) INCLUDING ROBOT HANDLING, CONVEYORS, ATON 1600, ETC. STILL INSTALLED, USED QUANTITY: 1 Learn More

REFERENCE NUMBER: T-6942 CEREAL PRODUCTION PLANT CEREAL PRODUCTION PLANT CORNFLAKES, EXTRUDED PRODUCTS, CRUNCHY MUESLI CAPACITY APPROX. 45 TONS / 24 HOURS STILL INSTALLED, USED QUANTITY: 1 Learn More

CAPACITY: 100 TO 150 MASKS PER MINUTE
PRODUCES MASKS WITH 3 LAYERS OF POLYPROPYLENE NONWOVEN MATERIAL
AIR PRESSURE: 0.6 MPa, AIR CONSUMPTION 300 LITERS PER MINUTE
CONTROLLED BY PLC, OPERATED BY LCD TOUCH SCREEN
USES ULTRASONIC WELDING FOR EAR STRAPS
VOLTAGE: AS PER CUSTOMER
TOTAL POWER: 11 KW
DIMENSIONS: 6850 x 3520 x 1990mm
WEIGHT: ≤ 5000kg

MASK SURFACE LAYER, FILTER LAYER AND BOTTOM LAYER CAN BE ALIGNED AND FED TO THE MACHINE AUTOMATICALLY
BOTH SIDES ARE SYMMETRICAL WITH ULTRASONIC PROCESS STATIONS FOR EAR STRAP WELDING
AFTER WELDING, THE MASKS ARE COUNTED AND PILED TOGETHER AUTOMATICALLY
MASKS ARE DISTRIBUTED EVENLY TO TWO SETS OF EAR STRAP STATIONS BY AUTOMATIC TRANSMISSION SYSTEM, CONTROLLED BY PLC
NOSE CLIPS CAN BE AUTOMATICALLY FED, CUT AND ULTRASONICALLY WELDED

THE CUP TYPE MASK PRODUCTION LINE CAN BE SENT BY AIR, THERE ARE TOTAL 5 WOODEN CASES, SIZES AND WEIGHT AS BELOW:

1. 2500 X 1100 X 1000mm, 1PC, 250KGS
2. 2200 X 1000 X 1500mm, 1PC, 1100KGS
3. 3000 X 1200 X 1500mm, 1PC, 1100KGS
4. 3000 X 1200 X 1500mm, 1PC, 1100KGS
5. 1900 X 700 X 1150mm, 1PC, 250KGS

IF CUSTOMER NEEDS MASK BAGGING MACHINE TO CONNECT WITH DISPOSABLE MASK PRODUCTION LINE, THERE WILL BE ANOTHER TWO WOODEN CASES EXTRA, BUT WILL CANCEL THE FIFTH WOODEN CASE, SIZES AND WEIGHT AS BELOW:

1. 1580mm X 840MM X 1510 mm，1PCS, 340KG
2. 2540 mm X 540 mm X 1510 mm，1PCS, 80KG

Learn More

R-6859 RE-ROAST 5-10

ROASTING MACHINES LINE, PARTICULARLY SUITABLE FOR LITTLE PRODUCTION ACTIVITIES OF HIGH QUALITY ROASTED COFFEE, SUCH AS SHOPS, PASTRIES OR ARTISANAL LABORATORIES.
SMALL SIZE, TECHNOLOGICALLY ADVANCED, CONFIRM THEMELVES AS IDEAL TOOL FOR THE PRODUCTION OF SELECTED COFFEES.

MADE WITH THE SAME REQUIREMENTS FOR RELIABILITY AND SECURITY FEATURES OF THE BIGGER AND MORE SOPHISTICATED INDUSTRIAL ROASTING MACHINES, ARE AVAILABLE WITH HEATING GENERATOR TYPE GAS BURNER (AVAILABLE ALSO BY ELECTRIC RESISTANCES) AND AUTOMATIC CONTROL SYSTEM WITH SEMIAUTOMATIC MANAGEMENT.

TECHNICAL DATA:
PATENTED ROASTING SYSTEM FOR HIGHER THERMAL EFFICIENCY ALLOWING
THE BEST POSSIBLE RESULT IN ROASTING COFFEE BY HOT AIR-CONVECTION.

HOPPER OF CHARGE STEEL MADE
HEATING GENERATOR BY GAS BURNER (AVAILABLE ALSO BY ELECTRIC
RESISTANCES)

COOLING TANK STAINLESS-STEEL MADE AND SELFCLEANING
INDEPENDENT MOTORISATIONS FOR ROASTING DRUM AND COOLING TANK
INDEPENDENT ELECTROVENTILATORS FOR ROASTING DRUM AND
COOLING TANK.

CICLONE-CHAFF COLLECTOR FOR CHAFFS SEPARATION
MACHINE COLOURS AVAILABLES ACCORDING CLIENT’S REQUEST.
NEW: AUTOMATIC UNLOADING SYSTEM AT THE END OF ROASTING CYCLE
NEW: ELECTRIC CONTROL BOARD WITH PLC + TOUCH-SCREEN WITH RECORDING OF ROASTING PARAMETERS.

Learn More

R-6857 TORREFACTO ROASTING MACHINES

THOR FKT
THE ROASTING MACHINE THOR FKT MB FOR ROASTED COFFEE WITH SUGAR IS BOUND AT HIGH HOURLY PRODUCTION. SINCE GREEN COFFEE IS ABLE TO OBTAIN A HOMOGENEOUS BAKING OF THE COFFEE IN 20 MINUTES FOR EACH CYCLE, WORKING IN AUTOMATIC MODE OR SEMI-AUTOMATIC.
THE ROASTING THOR FKT MB IS EQUIPPED WITH A STOVE DETACHED, BUILT IN STEEL AND REFRACTORY MATERIAL; THE BURNER, CAN BE GAS (TYPE MODULATING) OR OIL-IN 2/3 FLAME LEVELS, DEPENDING ON THE APPLICATIONS.
THE COOLING DRUM RECEIVES THE PRODUCT DIRECTLY FROM THE DISCHARGE OF THE ROASTING MACHINE.
THE INTERNAL MIXERS WERE DESIGNED AND TESTED IN ORDER TO GUARANTEE AN OPTIMAL COOLING OF THE PRODUCT.
THE DISCHARGE OF THE PRODUCT IS MADE BY REVERSING THE DIRECTION OF ROTATION OF THE DRUM; ON THE COOLING DRUM DOORS FOR THE INSPECTION AND CLEANING OF THE DRUM ARE PROVIDED.
ADDITIONAL FUNCTIONS OF ROASTING MACHINE THOR FKT MB:

POSSIBILITY OF TOTALLY OR PARTIALLY AUTOMATIC CONTROLLING BY PLC + TOUCH SCREEN AND SAVING PARAMETERS ROASTING PERFORMED BY ELECTROMECHANICAL/ELECTROPNEUMATIC DEVICES.
PLC WITH OPERATOR INTERFACE;
DISPLAY TO MONITOR THE FUNCTIONS OF ROASTING TIME AND TEMPERATURE;
AUDIBLE AND VISUAL ALARM ON THE MOTOR ALARM INSTALLED AND ON THE BURNER BLOCK.
COLOR: AVAILABLE ACCORDING TO CUSTOMER SPECIFICATIONS
OPTIONAL COMPONENTS:

ELECTRICAL CONNECTION MANAGEMENT SYSTEM WITH PC AND TOUCH-SCREEN
HEAT RECOVERY UNIT
POST-COMBUSTOR MODEL KAT
BRIQUETTE PRESS

Learn More

R-6854 BUHLER ROASTMASTER™20

THE ROASTMASTER™20 BY BUHLER OFFERS EXACTLY WHAT START-UP BUSINESSES AND SMALL-SCALE INDUSTRIAL OPERATIONS REQUIRE TO PRODUCE TOP-QUALITY COFFEE. THE CAPACITY RANGES UP TO 70 KG OF GREEN BEANS PER HOUR. HOT AIR IS THE BEST CHOICE TO ENSURE A UNIFORM ROAST. ALL HOT AIR PASSES THROUGH THE ROTATING DRUM AND TRANSFERS ITS HEAT DIRECTLY TO THE BEANS IN A HOMOGENEOUS WAY. THIS HOT AIR PATHWAY ENSURES A HIGH PROPORTION OF CONVECTIVE HEAT TRANSFER RATHER THAN TO HEAT THE DRUM FROM BELOW. NO MATTER AT WHICH STAGE OF THE PROCESS, THE VARIABLE DRUM SPEED AND THE SOPHISTICATED INTERIOR DESIGN OF THE ROASTING CHAMBER DELIVER AN OPTIMAL BEAN DISTRIBUTION AND AN EFFICIENT INTERACTION OF THE BEANS WITH THE AIR. SILVERSKINS ARE SEPARATED IN THE CYCLONE. THE COMPACT DRUM ROASTER IS EQUIPPED WITH SEPARATE HEATING AND COOLING FANS WHICH ALLOW TO ROAST AND COOL AT THE SAME TIME. AN INNOVATIVE AND EASY-TO-USE PLC CONTROL SYSTEM ENSURES QUALITY CONSISTENCY DURING PRODUCTION BUT ALSO LEAVES ROOM FOR MANUAL INTERVENTION TO STEER THE PROCESSING WHEN NECESSARY.

ROASTMASTER™20. PROCESS FLEXIBILITY FOR YOUR FLAVOR SIGNATURE.
EACH COFFEE VARIETY IS UNIQUE BY NATURE AND REQUIRES INDIVIDUAL ROASTING CONDITIONS TO TRANSFORM THE FULL INTRINSIC FLAVOR POTENTIAL INTO GREAT FLAVOR. THE ROASTMASTER™20 IS EQUIPPED WITH A FULLY VARIABLE BURNER FOR FLEXIBLE ENERGY INPUT. THE FREQUENCY CONVERTER ON THE MAIN FAN ALLOWS FOR VARIABLE SPEED AND OPTIMIZED AIR-TO-BEAN-RATIO DURING THE DIFFERENT STAGES OF THE PROCESS. REGARDLESS WETHER YOU PREFER TRADITIONAL OR NON-CONVENTIONAL PROFILES, THE SOPHISTICATED MULTISTEP PROCESS CONTROL SOFTWARE INSPIRES PROFILE ROASTING FOR BEST FLAVOR GENERATION.

DATA MANAGEMENT AND NEXT GENERATION CONNECTIVITY.
THE FUTURE-SAFE CONCEPT INCLUDES AN EASY-TO-USE PLC CONTROL SYSTEM WITH INTEGRATED TOUCH PANEL, RECIPE MANAGEMENT, ONLINE TREND MONITORING, BATCH REPORT CREATION AND SAFETY FEATURES. MOREOVER THE EASY DATA EXPORT VIA USB PORT, ONLINE DATA TRANSFER TO EXTERNAL THIRD PARTY PROCESS MONITORING SOFTWARE AND REMOTE HMI VISUALIZATION AND PROCESS CONTROL ENSURE QUALITY CONSISTENCY DURING PRODUCTION.

Learn More