# From risk to SIL: how a protection is sized

> SIL is not a label you pick, it is a level you calculate from the risk. Here is the chain of reasoning, from the hazard to the required integrity level — with the numbers.

- Source : https://industryhub.site/en/learn/safety/du-risque-au-sil
- Track : safety
- Level : Practitioner
- Reading time : 8 min
- Language : English

## In brief

The SIL (safety integrity level) is derived from risk: you assess the severity and probability of a hazardous scenario, derive the required risk reduction factor (RRF), and that factor sets the SIL. Each SIL maps to a PFDavg band; reaching that PFD depends on the components and the architecture.

## The SIL is not chosen, it is calculated

A common mistake: "let's go with SIL 3 to be on the safe side." The SIL is not a comfort level you buy, it is the result of a **calculation** that starts from the actual risk. Aiming too high is expensive and does not make things safer if the rest does not keep up; aiming too low leaves an unacceptable risk.

## The chain of reasoning

**1. Identify the hazard.** What serious event could occur? An overpressure, an overflow, a runaway reaction. We use structured methods such as the HAZOP (hazard and operability study).

**2. Assess the risk.** Risk combines two factors:

$$\text{Risk} = \text{Severity} \times \text{Frequency}$$

How severe are the consequences (injuries, fatalities, environmental damage)? How often can the scenario occur? You then compare with the **tolerable risk**, whose typical order of magnitude for individual risk is **10⁻⁴ to 10⁻⁵ per year**.

**3. Determine the necessary risk reduction.** The gap between the risk **without protection** and the **tolerable** risk is the risk reduction factor (RRF) the safety function must provide. The common method is the LOPA (layer of protection analysis).

## From the reduction factor to the SIL

Each reduction factor maps to a SIL, and each SIL maps to a band of average probability of failure on demand ($\mathrm{PFD}_{avg}$), linked by:

$$\mathrm{RRF} = \frac{1}{\mathrm{PFD}_{avg}}$$

| SIL | Risk reduction (RRF) | PFDavg (low demand) |
|---|---|---|
| SIL 1 | 10 – 100 | 10⁻¹ – 10⁻² |
| SIL 2 | 100 – 1,000 | 10⁻² – 10⁻³ |
| SIL 3 | 1,000 – 10,000 | 10⁻³ – 10⁻⁴ |
| SIL 4 | 10,000 – 100,000 | 10⁻⁴ – 10⁻⁵ |

These bands apply in **low-demand mode** (the function is called on less than once a year) — the process case. In **high-demand** or continuous mode, you no longer reason in PFDavg but in **PFH** (probability of dangerous failure per hour). The [risk reduction → SIL calculator](/en/tools/safety/rrf-sil) and the [PFD → SIL calculator](/en/tools/safety/pfd-to-sil) perform these conversions directly.

## PFD is built up, not decreed

Once the SIL is known, it becomes a **target** for the safety instrumented function (SIF), implemented by a safety instrumented system (SIS). The PFD of a SIF is the **sum** of its subsystems' contributions:

$$\mathrm{PFD}_{avg} = \mathrm{PFD}_{sensor} + \mathrm{PFD}_{logic} + \mathrm{PFD}_{final}$$

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  <text x="102" y="92" text-anchor="middle" font-size="12.5" fill="#5b6b69">PFD ≈ 1.2·10⁻³</text>
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  <text x="330" y="92" text-anchor="middle" font-size="12.5" fill="#5b6b69">PFD ≈ 2·10⁻⁴</text>
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  <text x="558" y="72" text-anchor="middle" font-size="15" font-weight="700" fill="#0b3b39">Final element</text>
  <text x="558" y="92" text-anchor="middle" font-size="12.5" fill="#5b6b69">PFD ≈ 4·10⁻³</text>
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  <text x="330" y="158" text-anchor="middle" font-size="14" font-weight="700" fill="#0b3b39">PFDavg ≈ 5.4·10⁻³ → SIL 2</text>
  <text x="330" y="182" text-anchor="middle" font-size="12.5" fill="#5b6b69">RRF = 1 / PFDavg ≈ 185</text>
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In this example the final element (the valve) dominates the PFD: it is almost always the weak link of a SIF, being the least reliable mechanical part. Reaching a SIL is therefore not just a number: it also requires the **architecture** (redundancy) and **robustness to failures**. A 1oo2 architecture tolerates one failure (hardware fault tolerance **HFT = 1**); the **SFF** (safe failure fraction) must also reach a minimum threshold imposed by the standard. This point is developed in the article [Functional safety and IEC 61508](/en/articles/securite-fonctionnelle-iec-61508).

## The mistake you must never make

Entrusting **protection** to the system that already handles **control**. The control loop that drives the process must not be the one that protects it: if it fails, you lose both at once. The safety system is **independent** of the control system — a fundamental principle, detailed in the [control loop](/en/learn/automation/boucle-de-regulation) and framed by the standards [IEC 61508](/en/standards/iec-61508) and [IEC 61511](/en/standards/iec-61511).
