Used Carbon Steel Converter; Surplus Carbon Steel Converter

10192 - USED SURPLUS CARBON STEEL CONVERTER
43'11" OVERALL; MULTI-LAYERED SHELL; FLG'D.; HEAD ON GROUND; VESSEL TEMP. RATED FOR -20 TO 430 F;

10207 - USED SURPLUS CARBON STEEL CONVERTER
PRIMARY CO CONVERTER; S/N C2827; (2) GRATE SUPPORTS INSIDE VESSEL; (3) PAK GRIDS; REVAMPED IN 1975 BY CHEMICO; 1"CHROMEMOLY; TOP HEAD 2.50"THK; BTM HEAD 1.437"THK;

10443 - USED SURPLUS CARBON STEEL CONVERTER
MFG BY A.O. SMITH; S/N B19646, 19463 & 2473; 41-1/4" OD.

16060 - USED SURPLUS CARBON STEEL CONVERTER
BUILT 1965; 40"ID; 6" GAS INLET; BASKET & SPARE BASKET OUT OF CONVERTER AND ON SKID; $175,000 W/SPARE BASKET;

35823 - USED SURPLUS CARBON STEEL CONVERTER
1ST & 2ND STG SHIFT CONVERTERS (2 VESSELS IN 1); DIVIDED BY 6'11" INTERMEDIATE SKIRT; 1962; S/N H-5004-62; HSB #17801; (R102)25'11" S/S, 310# @ 850F, TP-606#, 1-5/16" SHELL & 2:1 ELLIP HEADS @ BOTH ENDS & 1/2" THK ASME F&D HEAD IN MIDDLE; (R103)28'1" S/S, 278# @ 800F, TP-493#; 1-1/16" SHELL & 2:1 ELLIP HEADS; ON 8'2" SKIRT;

38576 - USED SURPLUS CARBON STEEL CONVERTER
AMMONIA CONVERTER; TAYLOR-FORGE, DIV. OF GULF & WESTERN 1971S/N 552626-1C; 1.448" HEMI BOTTOM HEAD; ON (5) LEGS; 41' OAHAPPROX 100 TPD OF NH3 THRUPUT; W/LADDER & SS CONVERTER BAS- KET; W/BASKET INSIDE OF CONVERTER; **PRICE IS COMPLETE W/BASKET**

80125 - USED SURPLUS CARBON STEEL CONVERTER
HALDOR TOPSOE DESIGN; RADIAL TYPE AMMONIA CONVERTER; SHELL MATERIAL C 1/2 MO; TOP COVER C 1/2 MO; HEMI BOTTOM HEAD 2 1/4 CR - 1 MO; PRESSURE SHELL: 84.5" INNER DIAMETER; 1073" INNER LENGTH (FROM INNERFACE OF TOP COVER TO SUPPORT OF BASKET); 3100 PSIG NORMAL OPERATING PRESSURE; 3555 PSIG DESIGN PRESSURE (MAX. OPERATING PRESSURE); 2318 PSIG HYDROGEN PARTIAL PRESSURE, DESIGN; TEMPERATURE OF: COVER AND CYLINDRIAL PART - OPERATING 260-295 DEG. F., DESIGN 500 DEG. F.; SPHERICAL BOTTOM - OPERATING 300-750 DEG. F.; DESIGN - 790 DEG. F.; BOTTOM FORGING - OPERATING 715 DEG. F.; DESIGN - 790 DEG F.; BOTTOM FLANGE - OPERATING 950-212 DEG. F.; DESIGN - 950 DEG. F.; BASKET: SERIES 200 TYPE; 1037 LENGTH OF OUTER SHELL; 498,452 LBS WEIGHT, CATALYST FILLED; INTERBED HEAT EXCHANGER 1-1 WITH DISC AND DOUGHNUT BAFFLES; 455 TUBES; 3/4" BWG TUBE DIMENSION; 1 1/6" PITCH; 204.75 EFFECTIVE LENGTH; 25.6" BAFFLE DISTANCE; 165.35" SHELL LENGTH; 26" SHELL ID; 17.492" DISC DIMENSION; 25.875/17.457" DOUGHNUT DIMENSION; INCONEL 600 TUBE MATERIAL; 304SS MATERIAL OF OTHER PARTS; NOTE: THE BAFFLE PLATES SHALL BE PROVIDED WITH PERFORATION HOLES, SIZE 0.3125"; LOWER HEAT EXCHANGER 1-1 WITH DISC & DOUGHNUT BAFFLES; 4044 TUBES; 3/4" BWG 16 TUBE DIMENSION; 1.00 PITCH; 67.5" EFFECTIVE LENGTH; 13.5" BAFFLE DISTANCE; 78.250" SHELL ID; 70.315" DISC DIAMETER; 78.00/33.622" DOUGHNUT DIAMETER; CATALYST BEDS: DIAMETERS: 1ST BED 70 7/8"/32 1/2", 2ND BED 73 1/4"/ 20 3/4"; TOTAL HEIGHT: 1ST BED 240", 2ND BED 684"; EFFECTIVE HEIGHT: 1ST BED 216", 2ND BED 648"; TOTAL VOLUME: 1ST BED 12.18 M CUBED, 2ND BED 43.35 M CUBED; EFFECTIVE VOLUME: 1ST BED 10.93 M CUBED, 2ND BED 40.91 M CUBED; CATALYST CHARGE: KMIR 1.5-3 MM, KMI 1.5-3 MM; KMIR 2140 KG/M CUBED BULK DENSITY, KMI 2150 KG/M CUBED BULK DENSITY; KMIR 12.18 M CUBED VOLUME, KMI 43.35 M CUBED VOLUME; KMIR 26100 KG TOTAL WEIGHT; KMI 119,200 KG TOTAL WEIGHT; ADDITIONAL INFORMATION: 25 DEG. F. LOWEST AMBIENT TEMPERATURE; 3100 PSIG MAX. OPERATING PRESSURE AT AMBIENT TEMPERATURE; "PRICE: AS IS, WHERE IS"