CHAPTER 06 / 06

Roasting Case Study: Venezuela (Washed / Medium-Dark City Roast)

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This document is an empirical log recording the roasting of a Venezuelan fully washed green coffee to a medium-dark (City) roast, executed in accordance with the Standard Process Guide.

  • Roast Date: August 18, 2026

Batch Specifications (Step 0)

Parameter Set / Measured Value Notes
Coffee Origin / Lot Venezuela Mucucay (2024/2025) -
Variety Castillo, Monte Claro, Caturra -
Processing Method Fully Washed -
Input Green Bean Weight 144.0g Standard unit (1kg bag divided into 7 batches)
Washing Water Temp 50°C (Purified water) Chaff and floater culling
Soaking Solution 50°C water + 15g honey + 20g fructose 30-minute soak
Post-Soak Bean Weight 190.3g Measured after removing 12.0g of defective floaters
Initial Bean Temp 28.7°C Infrared reading immediately before roasting
Initial Bed Volume 300–325ml Visual cylinder reading
Total Weight (incl. container) 459.4g -

Profile Projection
Consistent with typical washed coffees, the hydrated weight reached 190.3g (near the upper baseline limit). Because the objective is a medium-dark roast (City Roast), the profile was designed to supply sustained thermal energy through the mid-to-late stages.


Detailed Roasting Operations

Steps 1–2: Setup

Secure the lid on the container and place the cylinder vertically on the wooden chopsticks centered on the microwave floor.

Step 3: Initial Uniform Preheating (300W)

No. Power Exposure Agitation Interval Volume Trend Operational Notes
1 300W 60s 23s 325ml Preheating initiated
2 300W 60s 25s 325ml Steady temperature rise
3 300W 60s 25s 325–350ml Initial expansion from internal steam pressure
4 300W 60s 52s - Interval extended for intermediate weighing
  • Step 3 Cumulative Heat Input: 72k Ws (300W × 60s × 4 sets)
  • Step 4 Pre-check Metrics: Outer wall temp 90.2°C / Total weight 456.7g (Moisture loss: 2.7g)
  • Assessment: An outer wall temperature around 90°C and 2.7g moisture loss align cleanly with standard baseline criteria, indicating low thermal runaway risk. A standard 26- to 27-step profile was deployed.

Step 4: Primary Heating (High + 500W Medium Power)

Applied the "800W + 500W × 50s" alternating cycle designed for higher-moisture batches. The lid was burped (<1s) during each agitation interval.

No. Power Exposure Agitation Interval Volume Trend Operational Notes
5 800W 30s 35s 325ml+ Rapid temperature rise
6 500W 50s 30s 325ml 50-second pulse accumulates thermal mass
7 800W 30s 29s 325ml Thermal boost
8 500W 50s 32s 300–325ml Volumetric contraction commences with moisture loss
  • Step 4 Interval Heat: 98k Ws / Cumulative Total: 170k Ws

Step 5: Steady-State Heating (Crack Preparation via Medium Power)

Employed 500W × 50s in the first half to build energy, shifting to 600W × 40s in the second half to enhance thermal uniformity.

No. Power Exposure Agitation Interval Volume Trend Operational Notes
9 500W 50s 30s 300–325ml Continued moisture evaporation
10 500W 50s 26s 300ml Surface yellowing starts
11 500W 50s 31s 300ml- Shifting from yellow to light brown
12 600W 40s 22s 275ml+ Switched to 600W
13 600W 40s 28s 275ml Maximum volumetric contraction phase
14 600W 40s 28s 275ml Uniform brown color spreading
  • Step 5 Interval Heat: 147k Ws / Cumulative Total: 317k Ws

Step 6: Thermal Boost Driving into First Crack

Based on bed color and volume dynamics, another round of energy was deemed necessary to cleanly initiate the crack. Instead of the 30-second pulses used for lighter roasts, two sets of 600W × 40s were applied.

No. Power Exposure Agitation Interval Volume Trend Operational Notes
15 600W 40s 30s 275ml Driving temperature upward
16 600W 40s 26s 275ml+ First crack commences (volumetric turning point)
  • Step 6 Interval Heat: 48k Ws / Cumulative Total: 365k Ws

Step 7: Driving First Crack (800W / 600W Alternating Boost)

To maintain crack momentum and thoroughly transfer heat through to the bean cores, alternating sets of 800W × 20s and 600W × 20s were conducted.

No. Power Exposure Agitation Interval Volume Trend Operational Notes
17 800W 20s 29s 275–300ml Early first crack (isolated pops)
18 600W 20s 30s 275–300ml Latent heat transfer
19 800W 20s 27s 275–300ml First crack continuing
20 600W 20s 30s 300ml- Expansion progressing
21 800W 20s 30s 300–325ml First crack peak
22 600W 20s 32s 300–325ml First crack subsiding
  • Step 7 Interval Heat: 84k Ws / Cumulative Total: 449k Ws

Step 8: Finishing & Second Crack Development

Targeting a medium-dark roast (City to Full City boundary), the roast was taken cleanly into second crack.

No. Power Exposure Agitation Interval Volume Trend Operational Notes
23 600W 15s 21s 300–325ml First crack completely ended
24 600W 15s 25s 300–325ml Quiet period immediately prior to second crack
25 600W 15s 25s 300ml- Second crack commences (fine, sharp snaps)
26 600W 15s 0s - Second crack peak confirmed; terminated immediately
  • Step 8 Interval Heat: 36k Ws / Cumulative Total: 485k Ws

Step 9: Discharge and Rapid Cooling

Discharged immediately onto the cooling tray; recorded bean temperature and applied forced air cooling.

  • Discharge Bean Temperature: 226.9°C
  • Total Post-Roast Weight: 110.0g (Net yield after 0.8g defect culling: 109.2g)
Roasted Venezuelan coffee in the case study
Roasted Venezuelan coffee in the case study

Roast Summary

Evaluation Metric Measured Value
Total Steps 26 steps
Net Microwave Exposure Time 15 min 30 sec
Total Elapsed Time (incl. agitation) 27 min 31 sec
Discharge Bean Temperature 226.9°C
Finished Bean Weight 110.0g (76.4% of dry green weight)
Total Cumulative Energy 485k Ws
Time-Normalized Equivalent Energy 1057.54 kW/h
Venezuela roast profile chart, 18 August 2026
Venezuela roast profile chart, 18 August 2026

Technical Analysis

Completing in 26 steps with 485k Ws cumulative energy and a final discharge temperature of 226.9°C successfully captured the entry into second crack, delivering the intended medium-dark City roast profile with clean body and rich caramelization.

Even with a washed lot requiring substantial latent heat of vaporization, the time-normalized energy metric was 1057.54 kW/h, remarkably close to the empirical standard baseline (approx. 1,060 kW/h). The high reproducibility of this index underscores the reliability of thermal mass management in microwave coffee roasting.