Skip to content

Knowledge Center

Crushing screening plant noise exposure management

Crushing screening plant noise exposure management

Noise is managed through exposure normalised to eight hours, not through an instantaneous reading. Once an action value is crossed, handing out earmuffs does not close the duty: control at source comes first, organisation second, personal protection last.

Mobile vs stationary plant ROI comparison

Mobile vs stationary plant ROI comparison

Purchase price on its own settles nothing. Once reserve life, relocations per year and the repeat cost of foundations and erection sit in one present-value table, the gap between a mobile and a stationary plant can change direction within a few years.

How to plan crushing plant lead time and shipment realistically

How to plan crushing plant lead time and shipment realistically

Lead time is not one number but the sum of four blocks that wait on each other: configuration freeze, manufacturing, site preparation and transport. Road gauge limits and customs paperwork are the two items buyers underestimate most often.

Plant Mix Road Base Gradation Compliance

Plant Mix Road Base Gradation Compliance

Plant mix base material is rejected far more often for uncontrolled blend ratios and moisture than for anything the machinery did. This article walks through the test methods behind the sieve curve, where deviation from the approved mix formula is caught, and which three records a shift must keep before compaction begins.

Manganese Steel Alloy Selection for Crusher Liners

Manganese Steel Alloy Selection for Crusher Liners

Two different manganese alloys bolted into the same frame will not last the same number of tonnes. This article matches work-hardening rate to feed hardness and impact energy, and shows in a table that the price of a harder surface is brittleness.

Choke Feeding Crusher Productivity

Choke Feeding Crusher Productivity

With the chamber kept full, rock breaks against rock: product turns cubical, liner wear spreads around the circumference and power draw flattens. Starved feed distorts shape and concentrates wear. Holding the level is a feeder and sensor job, not a wish.

Screen efficiency and screen area sizing

Screen efficiency and screen area sizing

A screen is not chosen from a catalogue. First the efficiency of the existing deck is measured with a sieve analysis, then the required area is derived from basic capacity and correction factors. This article puts the two-product formula, the sizing factors and the bed-depth limit in one place.

Crushing plant environmental noise limits and barriers

Crushing plant environmental noise limits and barriers

Noise limits apply at the nearest sensitive building, not at the machine; a point source loses six decibels each time distance doubles, and a barrier only works once it breaks the line of sight.

Respirable Crystalline Silica Exposure Crushing Plant Guide

Respirable Crystalline Silica Exposure Crushing Plant Guide

The dangerous part of quarry dust is not the visible cloud but the fine fraction that reaches the alveoli. Limits, personal sampling with a cyclone, engineering controls, respirator classes and health surveillance, set out in one place.

Crusher Total Cost of Ownership

Crusher Total Cost of Ownership

Purchase price is a small share of what a crusher will cost you over its life. This article builds the skeleton of a ten-year ownership model: which line items belong in it, which record feeds each one, and which assumptions the cost per tonne is genuinely sensitive to.

Letter of credit for crushing plant purchase

Letter of credit for crushing plant purchase

On a crushing and screening order the payment instrument decides how non-delivery, non-payment and delay risk is split between the two sides. This guide compares irrevocable and confirmed credits, documents against payment and the advance payment guarantee, and lists the documents that belong in the credit text.

Rebar Separation When Crushing Reinforced Concrete

Rebar Separation When Crushing Reinforced Concrete

Steel embedded in demolition concrete is the single most expensive contaminant a recycling line handles: it wraps the rotor, wedges the chamber and breaks wear parts. This article sets out where the steel is taken out, with which equipment, and in what order, so the machine is protected and the scrap becomes revenue.

Wear Part Life Tracking Method

Wear Part Life Tracking Method

Life is counted in tonnes passed, not in days. Thickness readings from fixed points, weighing at fitting and removal, a wear rate per tonne and the remaining allowance divided by that rate give a change window you can plan around.

Shift production report crushing plant

Shift production report crushing plant

What gets written at the end of the shift decides what can be improved next quarter. Here is the field structure, the downtime code set, the tonnage reconciliation and the weekly review that makes the record pay for itself.

Closed Circuit Circulating Load Crushing: Sizing the Real Feed

Closed Circuit Circulating Load Crushing: Sizing the Real Feed

In a closed circuit the crusher always sees more tonnage than the plant produces, and the difference is the returning oversize. This article shows how that multiplier is calculated, how screen efficiency inflates it, and why a tertiary machine has to be selected on total feed rather than on fresh feed.

Baghouse jet pulse dust collector selection for crushing plants

Baghouse jet pulse dust collector selection for crushing plants

Dry dust extraction is decided by three numbers: the air volume to be drawn, the filter area it passes through, and the ratio between them. For mineral dust that ratio sits in a narrow band, and pushing past it costs bag life and stable pressure drop. This article sets out the band and the hood geometry that feeds it.

Crusher emergency stop pull cord system

Crusher emergency stop pull cord system

A pull cord breaks the hazard chain in one movement, but it only works if the rope reaches every point, slack is detected and resetting never restarts the machine. An untested chain protects nobody.

Aggregate production cost per ton

Aggregate production cost per ton

Cost per ton is not one figure but the sum of six components. This piece shows what data measures each one, how often it is read, and why the denominator must be saleable tonnage rather than rated capacity.

Incoterms for crushing equipment export FOB vs CIF

Incoterms for crushing equipment export FOB vs CIF

A delivery term is not a price line; it states where risk changes hands. An out-of-gauge crusher body and a container of wear parts will not tolerate the same rule, so the choice follows cargo type and which side actually controls the freight.

On-site concrete demolition crushing workflow

On-site concrete demolition crushing workflow

Demolition concrete processed where it falls avoids paying twice: once to haul it away and once to buy fill. A workflow that pins pre-sorting, feeding, crushing, screening and stockpiling to shift hours turns a rubble pile into measured tonnes by close of day.

Crushing plant vibration analysis as the base of predictive maintenance

Crushing plant vibration analysis as the base of predictive maintenance

Vibration measurement is the only practical way to tell imbalance, misalignment, a loose anchor bolt and bearing damage apart on a crushing circuit. An overall reading alone will not do it; without a spectrum read against shaft speed, an alarm is just a number.

Cost Per Ton Crushing Breakdown

Cost Per Ton Crushing Breakdown

Cost per ton in a crushing and screening plant never arrives as a single invoice. It is assembled from five separate items that must be reduced to the same production period. This article separates fixed from variable behaviour, names the record each item comes from, and shows how to verify the tonnage that goes in the denominator.

Crushing Circuit Mass Balance

Crushing Circuit Mass Balance

Feed tonnage splits at the screen, oversize returns to the crusher and the rest reports to stockpiles. This article derives every stream in tonnes per hour from a 200 t/h feed and ties belt width and stockpile area to that table.

Fog Cannon vs Water Spray Dust Suppression

Fog Cannon vs Water Spray Dust Suppression

Capture probability rises as droplet size approaches the size of the dust being targeted. A fan-driven cannon covers open areas, a nozzle line suppresses dust at the source with far less water, and winter drainage decides which one survives on your site.

A crushing and screening plant is a chain, not a shopping list

An aggregate operation is never the sum of the machines parked on its pad. It is an uninterrupted chain that begins with the character of the rock in the quarry face and ends when the last graded fraction lands on the stockpile. A poor decision taken in one link rarely announces itself where it was made. An abrasiveness figure nobody measured turns into an unbudgeted wear-part invoice two seasons later. A conveyor sized too tightly during layout quietly caps shift tonnage for the working life of the plant. A calibration skipped at commissioning settles in as years of lost screening efficiency. The Knowledge Center is therefore organised around the lifecycle of the investment rather than around machine families.

The six stages below describe the decision points that genuinely follow one another on site. Each stage has its own questions, its own measurable quantities and its own specialist. The eight subject areas lie across this cycle. None of them explains the plant on its own, yet read together they cover most of the choices an owner faces over the economic life of the investment.

1. Quarry and feed definition

Everything starts with knowing what the rock is. Basalt and limestone can pass through the same feed opening, yet they do not deserve the same flowsheet. Hardness, abrasiveness, clay and moisture content, muckpile fragmentation after the blast and top block size directly determine the primary crusher type, the feeder selection, the number of screen decks and whether washing is needed at all. If the data produced at this stage is wrong, every later calculation rests on unstable ground. Sampling discipline, how laboratory results should be read and the places where field observation contradicts the laboratory all belong under this heading.

2. Plant layout and flowsheet

Once the feed is characterised the question changes: which crushing stages, in which order, balanced at which capacity? Whether the primary stage should use a jaw crusher or an impact solution, how the choice between a cone crusher and an impactor in the secondary stage shifts particle shape and wear cost, the ratio of screening area to throughput, and the logic behind stockpile placement are all settled here. The most expensive layout mistake is imbalance: when one stage runs faster than the next, total plant output locks onto the slowest link.

3. Installation and commissioning

Foundations, chassis levels, conveyor angles, the electrical room and the dust extraction connections are fixed at this stage in ways nobody revisits for years. Commissioning is not merely starting the machine. It means logging no-load current values, writing down setting ranges as a reference and taking the first gradation measurement. Without those baseline records you will hold no evidence, two years later, of whether the plant has genuinely slowed down or whether expectations alone have risen.

4. Operation and production management

The moment the plant produces, the questions become economic: how many tonnes per shift, how many kilowatt-hours per tonne, which fraction is overproduced and which one cannot be sold? Feed continuity, crushing chamber level, screen blinding and stockpile balance turn into daily decisions. The production manager's strongest tool is consistent recording of the measured quantities; in a plant run on instinct the bottleneck appears to move every shift.

5. Maintenance and wear management

A wear part is a planning instrument, not a cost line. Knowing in advance when the jaw plate, the blow bar or the mantle and concave will reach the end of their service life means placing the stoppage inside a planned maintenance window. Unplanned downtime always costs more than the component itself: lost production, an idle crew and a late delivery meet on the same invoice. Lubrication schedules, vibration monitoring and honest part-life records form the backbone of this area.

6. Compliance, safety and environment

The final link is the plant's permission to keep working. Machine guarding, energy isolation and lockout practice, the reachability of emergency stop lines, whether dust suppression truly performs under load, and the management of noise and water together protect both worker health and the operating licence. In most projects this area is left until last, although it is the cheapest one to handle while the layout is still on paper.

The eight subject areas and where they sit in the cycle

The table below summarises the question each area begins with, the decision point at which it becomes relevant and the quantity it measures. Follow a heading to reach every article filed under that area.

Subject areaTypical questionDecision pointQuantity measured
Mining EngineeringWhat flowsheet does this rock deserve?Quarry planning and feed definitionHardness, abrasiveness, block size, gradation
Plant EfficiencyWhere is the bottleneck really?Operation and shift managementTonnes per hour, utilisation, kWh per tonne
Maintenance and WearHow much longer will this part last?Planning the maintenance windowPart life, unplanned downtime, oil and vibration readings
Jobsite and Mobile PlantMove the plant or fix it in place?Site setup and works programmeSetup time, number of relocations, footprint
Procurement and SupplyAre these quotations genuinely comparable?Order and contractLead time, spare part access, warranty scope
Investment and CostHow does this plant pay for itself?Investment decision and budgetingTotal cost per tonne, capital against operating balance
Occupational SafetyHow is this task carried out safely?Procedure writing and site auditGuard integrity, lockout compliance, incident records
Environment and Dust ControlDo the permit conditions match site reality?Permit application and routine inspectionDust emission, noise, water use and recovery

Capacity decisions begin with concrete figures

So that the second and third links of the cycle do not stay abstract, the catalogue values of our mobile plant family are set side by side. The table shows which model corresponds to which feed size and which capacity band; the largest block leaving the face meets the target shift tonnage where these two columns intersect.

ModelMaximum feed sizeCapacityOutput size settingOptional generator
General 640500 mm40-70 t/h0-100 mm300 kVA
General 800600 mm80-120 t/h0-100 mm450 kVA
General 01700 mm120-180 t/h0-100 mm550 kVA
General 950800 mm120-180 t/h0-100 mm600 kVA
GNR-MC110900 mm200-300 t/h0-100 mm750 kVA

The product sizes listed belong to the standard configuration and can be changed on request. As feed size grows, so do the primary opening and the drive power; the capacity band, however, depends not only on the machine but on how steady the feed is and how readily the material breaks. The same model works at the upper end of its band in an easily crushed limestone and at the lower end in hard, abrasive rock.

How to use this centre

Identify the stage your investment has reached and start from the subject area that governs it. If no machine has been chosen yet, narrow the field by rock type and target capacity with the product selection wizard, then test the economics with the operating cost calculator. Any term met in these articles can be checked quickly in the technical glossary.

Every article here is drawn from field practice; these are decision-support notes rather than textbook chapters. After reading one, compare it against your own plant data, note the point where the two diverge and send that note to our engineering team. If your quarry conditions call for a dedicated flowsheet, reach us with your rock analysis and target fractions so the assessment rests on a concrete capacity balance table instead of assumptions.

Frequently Asked Questions

Who is this centre written for?

It is written for the people who actually sign off decisions on an aggregate plant: quarry and process engineers, production managers, maintenance leads, buyers and owners. Each subject area speaks to one of those roles without assuming the others have already explained the context.

How does this differ from the product pages?

A product page describes what one machine does and the specification it works to. The centre deals with the choice between machines and the consequences of that choice further down the chain, which is a different question with different evidence behind it.

Do the capacity figures apply to my material?

The feed opening and the setting range are fixed limits of the machine. The capacity band is not fixed: it moves towards the upper figure in easily crushed material and towards the lower figure in hard, abrasive rock. Where your material sits inside that band is decided by analysis.

The plant is already running. Where should I start?

Start with Plant Efficiency to locate the bottleneck with measured numbers rather than impressions, then move to Maintenance and Wear if the losses turn out to be stoppage-driven. Reading them in that order avoids replacing a component that was never the constraint.

Can our existing flowsheet be reviewed?

Yes. Send the rock analysis, the current stage arrangement and the fractions you need to sell. The review is returned as a capacity balance across the stages, which shows where the chain is unbalanced before any equipment change is proposed.