Polokwane’s Industrial Park area carries the kind of work where gas stops being a utility and becomes part of the production process — burners on ovens, dryers, kilns and heat-treatment equipment. On these sites the pipework is the straightforward half of the job. The engineering that matters sits in the gas train, the combustion controls and the interlocks that decide whether the burner is allowed to light at all.
Process burner or industrial oven installation? Send the equipment data sheets.
Get Process Gas QuotesThe Gas Train and Combustion Controls
What sits between the supply and the burner head determines whether an installation is genuinely safe, and it is where quotes differ most.
- Double safety shut-off valves with proving are standard on industrial burners and are not the place for a cheaper alternative
- Flame supervision ensures the gas stops if the flame is lost, and its response time is a specification, not a detail
- High and low gas pressure switches prevent the burner operating outside the range it was commissioned for
- Air proving interlocks stop the burner firing without combustion airflow, which is the failure mode that fills an enclosure
- Purge sequences before ignition clear any accumulated gas, and skipping them to speed up a cycle is how explosions happen
Sustained process draw? Get vaporisation sized properly rather than by volume.
Request a Vaporisation AssessmentAltitude, Combustion Air and Commissioning
Polokwane sits around 1,300 m above sea level, and on industrial burners that has consequences most sea-level commissioning data does not account for.
- Air density at altitude is meaningfully lower, so a burner set to default figures receives less combustion air than intended
- Manufacturers generally publish derating data or supply alternative injectors, and both need requesting rather than assuming
- Symptoms of a missed correction are sooting, flame instability, reduced output and poor efficiency rather than an outright failure
- Flue sizing and draught are affected by the same air density change and should be checked with the burner
- Commissioning records should state the altitude corrections applied, so the next engineer is not guessing
Continuous Draw and Vaporisation
Process equipment runs for hours rather than minutes, and that changes the storage question from how much to how fast.
- Volume determines delivery frequency; vaporisation rate determines whether the system works at all — installations fail the second while passing the first
- Frost on the vessel is the diagnostic. It means demand is outrunning vaporisation, not that you are running out of gas
- Ambient temperature drives vaporisation, so a system that copes in a Polokwane January can fall short on a July morning
- A vaporiser decouples output from ambient conditions and is far better designed in than retrofitted once the pressure problem appears
- Size for the production ceiling, not for current output, because adding capacity to a live process line is disruptive
Flues, Ventilation and the Enclosure
An industrial burner is only as safe as the air arrangements around it, and those are part of the gas installation rather than a separate trade’s problem.
- Combustion air supply must be calculated for the total connected load and remain unobstructed in practice, not just on the drawing
- Flue routing, termination and material selection depend on the flue gas temperature and the equipment type
- Direct-fired and indirect-fired arrangements have different implications for the process atmosphere and product contamination
- Extraction systems interact with combustion air, so a change to one requires reviewing the other
- Dust in a Polokwane industrial environment fouls air inlets and burner components, which makes filtration and cleaning intervals a design decision
Commercial Gas Installation Services in Industrial Park
Full range of industrial LPG work across Industrial Park and neighbouring Superbia, Magna Via, Laboria, Ladine and Nirvana Industrial:
Certificates and Compliance for Industrial Park Sites
Industrial installations carry a documentation burden well beyond the certificate. Auditors, insurers and often customers will ask for as-built drawings showing routes, diameters, isolation and test points, the load calculations behind the design, strength and tightness test records, and the equipment documentation for regulators, burners, vaporisers and safety devices.
Insist on that pack at handover. On a large site reconstructing it afterwards is a substantial exercise, and the moment it is usually needed is the moment nobody has time to assemble it. Commissioning records should include the altitude corrections applied, which is a detail that saves an engineer real time years later.
Industrial Gas Installation Costs in Industrial Park
Process installations sit in a different pricing bracket from catering work, and the reason is the gas train rather than the pipe. Safety shut-off valves, flame supervision, pressure proving and the associated control and electrical work make up a large share of the cost of a properly engineered burner supply.
When comparing quotes, compare the control specification line by line before comparing totals. A significantly cheaper industrial quote is usually cheaper in exactly the place you least want it to be, and the difference is not visible once the panel door is closed.
Ballpark Costs by Type of Job
For components with published South African pricing, indicative ranges follow. Larger work is quoted after a site survey.
| Type of job | Indicative range | What moves it |
|---|---|---|
| Single appliance connection Adding one unit to an existing line | R1 500 – R8 000+ | Length of new pipework, whether the existing line and regulator can carry the extra load, accessibility of the drop point. |
| Certificate of Conformity Inspection and testing only | From roughly R750 – R950, plus about R150 per additional appliance | Number of appliances, how accessible the pipework is, and whether the system holds a tightness test first time. Remedial work is quoted separately. |
| Gas cage / cylinder compound | R1 450 – R3 750+ | Cylinder count, whether a plinth, bollards or screening are needed, and whether it is fabricated on site. |
| Regulators | R200 – R3 000+ per unit | Single versus two-stage, capacity required at peak draw, and whether automatic changeover is included. |
| Commercial kitchen gas line Multi-appliance line with cylinder bank | Quoted per site | Total connected load, number of drops, pipe diameter and run length, bank size, manifold and changeover, cage, testing and certification. |
| Cylinder bank upgrade Adding capacity or auto changeover | Quoted per site | Cylinder positions added, changeover type, whether the existing pipework and regulator can carry the higher flow. |
| Bulk LPG tank installation | Quoted per site | Vessel size, base and civils, separation distances, tanker access, distance to the point of use. |
| Leak investigation | Quoted per site | Size of the installation, whether sectional isolation exists, and whether any of the run is buried or concealed. |
Published market figures only, exclusive of cylinders, gas and VAT.
Send burner data sheets, a site plan and your production schedule.
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