Crane Selection for Oil Refineries: Kelude, FCC & Storage

In brief: Kelude Heavy Industry provides crane configuration solutions for oil refineries covering four key zones—atmospheric/vacuum distillation, catalytic cracking, hydrotreating, and storage & loading—with lifting capacities from 5 to 120 short tons (4.5 to 109 metric tons) and spans from 12 to 36 m (39 to 118 ft). Total crane equipment investment ranges from approximately $89,000 to $890,000. The atmospheric/vacuum distillation zone is equipped with explosion-proof overhead cranes (20–50 short tons / 18–45 metric tons), the catalytic cracking zone uses high-temperature-resistant explosion-proof overhead cranes (30–80 short tons / 27–73 metric tons), the hydrotreating zone is fitted with stainless steel anti-corrosion explosion-proof cranes (10–30 short tons / 9–27 metric tons), and the storage zone uses explosion-proof overhead cranes (10–20 short tons / 9–18 metric tons)—all engineered to meet lifting and hoisting requirements in high-temperature, high-pressure, hydrogen-sulfide-corrosive, flammable, and explosive environments.

Crane Selection Solutions for Oil Refineries

Atmospheric/Vacuum Distillation | Catalytic Cracking | Hydrotreating/Hydrogen Production | Storage & Loading

Oil refineries are among the most demanding environments for lifting equipment in the petrochemical industry.

Oil Refinerycrane selectionSolution——Atmospheric and Vacuum Distillation/Fluid Catalytic Cracking (FCC)/Hydrotreating / Hydrogenation/Four Storage & Transportation Zones

Zone 1: Atmospheric/Vacuum Distillation

• Lifting capacity: 10–50 short tons (9–45 metric tons), explosion-proof LH type overhead crane

• Explosion-proof rating: Ex d IIB T4

Ex d IIB | Maintenance Lifting

Zone 2: Catalytic Cracking

• Lifting capacity: 20–80 short tons (18–73 metric tons), explosion-proof QD type overhead crane

• Explosion-proof rating: Ex d IIB T4

Large Tonnage | Catalytic Unit Maintenance

Zone 3: Hydrotreating/Hydrogen Production

• Lifting capacity: 10–32 short tons (9–29 metric tons), explosion-proof overhead crane

• Hydrogen-rated explosion-proof: Ex d IIC

Hydrogen Explosion-Proof | Sealed Anti-Corrosion

Zone 4: Storage & Loading

• Lifting capacity: 3–16 short tons (2.7–14.5 metric tons), explosion-proof hoist

• Explosion-proof rating: Ex d IIB T4

Oil-Product Explosion-Proof | Tank Farm Maintenance

Selection Parameters Across the Four Zones

Parameter ItemAtmospheric and Vacuum DistillationFluid Catalytic CrackingHydrotreating/Hydrogen ProductionStorage & Loading
recommended modelExplosion-proof LH TypeExplosion-proof QD Typeexplosion-proof overhead crane/HoistExplosion-proof electric hoist
Lifting Capacity10t~50t20t~80t10t~32t3t~16t
Work Duty / ClassificationA4~A6A6~A7A5A3~A5
Explosion Protection ClassEx d IIB T3Ex d IIC T3Ex d IIC T3+H₂SAnti-corrosionEx d IIB T4
special requirementsHigh Temperature Resistant80℃High Temperature Resistant100℃+Wear-ResistantNACE MR0175Anti-SSCExplosion-proof+anti-static
Kelude Schemeheat-resistant+HGradeinsulationWater-Cooled Electrical Control+thermal insulation layer316L+HICSteel Plateexplosion-proof certification+hermetic motor
$890K–$8.9M
Total crane equipment investment
5–120 t
Lifting capacity range
12–36 m
Crane span range
Ex d IIC T3
Refinery explosion protection class
C5-I
H₂S corrosion protection rating
5–20 million t/yr
Typical refinery production capacity

Kelude Distillation and Fluid Catalytic Cracking

Refineries are among the most crane-intensive facilities in the petrochemical industry.

During operation of the crude distillation unit, overhead cranes are primarily used for maintenance and replacement of overhead condensers (10–25 t), air cooler tube bundles (5–15 t), and process pumps (2–8 t). A 20/5 t or 32/5 t explosion-proof bridge crane is recommended for this service. For the FCC unit, regenerator and settler maintenance calls for a 50/10 t high-temperature-resistant explosion-proof overhead crane (span 24–36 m, A6), with forced-air cooling and a double-layer insulated housing on the electrical control box. The cyclone separator liners inside the regenerator and settler (3–8 t) are replaced every 2–3 years and require a specialized spreader for safe removal and installation.

Hydrotreating and Tank Farm Lifting Solutions

In a typical 1 million t/yr diesel hydrotreater, the core lifting tasks include catalyst loading/unloading for the hydrotreater reactor (empty weight 50–120 t; catalyst is replaced every 1–2 years, with 30–80 t of catalyst charged per cycle using a catalyst suction system), tube bundle extraction for high-pressure heat exchangers (20–40 t), and replacement of high-pressure air cooler bundles (10–20 t). Kelude recommends a 20/5 t or 32/5 t explosion-proof and anti-corrosion bridge crane (Ex d IIC T3, C5-I anti-corrosion) with a span of 24–30 m for the hydrotreating unit. During catalyst loading, the crane must handle the catalyst hopper (3–5 t) and the reactor top cover (4–8 t). Because hydrotreating units operate at high pressure (8–20 MPa) and contain H₂S (1%–5% concentration), the crane must be designed for sulfide stress cracking (SSC) resistance in accordance with NACE MR0175.

The core lifting tasks in a hydrotreating unit (using a 1 million t/yr diesel hydrotreater as an example) include catalyst loading/unloading for the hydrotreater reactor (empty weight 50–120 t), tube bundle extraction for high-pressure heat exchangers (20–40 t), and replacement of air cooler tube bundles (10–20 t). Kelude recommends a 20/5 t or 32/5 t explosion-proof and anti-corrosion bridge crane (Ex d IIC T3, C5-I anti-corrosion) with a span of 24–30 m. In the tank farm, the main lifting requirements for both crude oil and product storage areas are tank maintenance (floating roof 5–15 t) and pipe rack installation. For tank areas, Kelude recommends an LD-type explosion-proof single-girder electric crane (Ex d IIB T4) or an explosion-proof electric hoist underslung crane, with a lifting capacity of 3–10 t.

In the crude oil tank farm (100,000 m³ external floating roof tanks, 80 m diameter) and product tank farm, crane requirements center on tank maintenance (floating roof repair 5–15 t, central drain pipe replacement 1–3 t) and pipe rack installation (single pipe sections 20 m long, 2–5 t each). Kelude recommends an LD-type explosion-proof single-girder bridge crane (Ex d IIB T4) or an explosion-proof electric hoist underslung crane (for pipe rack areas) with a lifting capacity of 3–10 t. During tank maintenance, the crane must work with a tank wall manhole platform using a specialized boom or jib crane. The explosion protection class for tank farm areas is typically designed to IIC T3–T4 (depending on the stored medium — gasoline Ex d IIB T3, diesel Ex d IIB T4, jet fuel Ex d IIC T3). For floating roof maintenance, the crane must be positioned outside the fire dike, using a long-reach spreader to lift over the dike for the hoisting operation.

Hydrotreating and Tank Farm Lifting Solutions

The core lifting tasks in a hydrotreating unit (using a 1 million t/yr diesel hydrotreater as an example) include catalyst loading/unloading for the hydrotreater reactor (empty weight 50–120 t), tube bundle extraction for high-pressure heat exchangers (20–40 t), and replacement of air cooler tube bundles (10–20 t). Kelude recommends a 20/5 t or 32/5 t explosion-proof and anti-corrosion bridge crane (Ex d IIC T3, C5-I anti-corrosion) with a span of 24–30 m. Because the hydrotreating unit operates at 8–20 MPa and contains H₂S (1%–5% concentration), the crane must be designed for sulfide stress cracking resistance in accordance with NACE MR0175.

In the storage and logistics area, the crude oil tank farm (100,000 m³ external floating roof tanks) and the finished product tank farm primarily require crane services for tank maintenance (floating roof sections weighing 5–15 t) and pipe rack installation. Kelude Heavy Industry recommends the LD Type explosion-proof electric single-girder crane (Ex d IIB T4) or an explosion-proof electric hoist underslung crane (for pipe rack areas), with lifting capacities from 3 to 10 t. During tank maintenance, the crane must work in conjunction with a dedicated boom through the tank wall manhole platform. The explosion protection class for the storage area is determined by the stored medium — gasoline: Ex d IIB T3, diesel: Ex d IIB T4, jet fuel: Ex d IIC T3.

Kelude Heavy Industry — Service Advantages for Refinery Cranes

Kelude Heavy Industry has years of experience serving the petroleum refining sector, supplying explosion-proof, corrosion-resistant crane solutions for major processing units such as atmospheric and vacuum distillation, fluid catalytic cracking, hydrocracking, and delayed coking. We hold petrochemical maintenance qualifications and Ex explosion-proof certification, with products covering the full lifting workflow from raw material handling to finished product storage.

High-Temperature Explosion-Proof Solutions for FCC Units
A: The reactor-regenerator system in an FCC unit operates at 500–700°C, with ambient temperatures around catalyst transfer lines often exceeding 100°C. Kelude Heavy Industry applies a triple-layer heat-resistant design: special heat-resistant steel structure, ceramic fiber thermal insulation layer, and Class H insulated motors. The electrical control box features forced air cooling with a double-wall insulated housing, ensuring safe and reliable crane operation under the extreme thermal conditions of an FCC unit.
H₂S Corrosion Protection for Hydroprocessing Units
A: Hydrotreating and hydrocracking units present dual corrosion risks from high-pressure hydrogen (8–20 MPa) and hydrogen sulfide (H₂S content 1%–5%). Kelude Heavy Industry's heavy-duty anti-corrosion solution uses a SUS316L stainless steel main structure, Inconel 625 alloy hooks, and PTFE-coated wire rope. All seals are made of perfluoroelastomer (FFKM), and the electrical cabinet uses nitrogen-purged positive-pressure explosion protection, delivering resistance to sulfide stress cracking in wet H₂S environments.
Turnkey Hoisting Services for Plant Turnarounds
A: Refineries typically conduct a full-plant turnaround every 3–4 years, involving extensive lifting operations such as reactor catalyst replacement, tower maintenance, heat exchanger bundle extraction, and pipeline replacement. Kelude Heavy Industry provides centralized crane support for turnarounds — completing inspection and maintenance of all cranes 45 days in advance, deploying on-site technical staff during the turnaround, and pre-stocking spare parts according to a detailed checklist to ensure seamless lifting operations throughout.

Frequently Asked Questions

Q: What lifting capacity is required for maintenance of the atmospheric tower in a crude distillation unit?
A: During operation, the overhead crane is primarily used for servicing the tower-top condensers (15–25 t) and air cooler tube bundles (8–15 t). Kelude recommends a 20/5 t or 32/5 t explosion-proof overhead crane (Ex d IIC T3) with coverage spanning the atmospheric tower, vacuum tower, and air cooler platforms. Tray removal is carried out through the tower-top manhole with the assistance of a hoist. The span in the heat-integrated section between the atmospheric and vacuum towers must also cover the heat exchanger and hot oil pump areas.
Q: What are the safety precautions for FCC regenerator maintenance?
A: The regenerator contains catalyst and CO gas at 600–700°C. Before maintenance begins, the following steps are mandatory: fully drain and cool the catalyst to below 60°C, steam purge until CO levels drop to ≤50 ppm, verify oxygen content is ≥19.5%, and obtain a confined space entry permit. The crane is used solely to assist with lifting and transport of maintenance tools and refractory lining materials. A restricted access zone must be established around the operating area during catalyst loading and unloading. H₂S and combustible gas concentrations must be monitored every 2 hours.
Q: What are the material selection standards for cranes in H₂S environments at hydrogenation units?
A: For wet H₂S environments in hydrogenation units, compliance with NACE MR0175 is required: load-bearing components use Q345R+HIC steel plate (CLR≤5%), hooks are made of 20MnMoNb with quenching and tempering and a hardness of ≤HRC22 (to prevent SSC), low-hydrogen welding electrodes are used (diffusible hydrogen ≤5ml/100g), and fasteners are 35CrMoA with cadmium plating or 316L Stainless Steel. The entire crane undergoes stress-relief heat treatment (580~620℃), and all Weld Seams receive 100% MT+UT Detection.
Q: How are cranes dispatched during a full-plant refinery overhaul?
A: ① Complete annual inspections and load tests on all cranes 60 days before the overhaul begins; ② Submit equipment status reports 30 days prior; ③ During the overhaul, assign one on-site coordinator for every 10 cranes, with daily inspections at 8:00 AM; ④ Spare parts—standard items delivered within 48 hours, specialty items within 72 hours; ⑤ Hold daily coordination meetings to review crane performance across units, with particular focus on the catalytic cracking and hydrotreating units.

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