For projects where the seed is already known and the next question is how the hydraulic press fits inside a workable line.
A rapeseed line is rarely just a press. The cooker, the refining train, and the cake handling path together define the project; the press is one node in that system.
The variety must be identified at intake — they look similar but produce different oils. Traditional Brassica napus / Brassica juncea high-erucic varieties versus canola (Canadian-bred low-erucic, low-glucosinolate). This determines the entire downstream plan.
Steam-jacketed cooker conditions the seed before hydraulic pressing. Proper conditioning gives cleaner oil release, lower residual oil in cake, and the characteristic nutty aroma traditional buyers expect.
300 ton hot-press for moderate capacity, 325 ton for higher-pressure handling of stubborn seed batches. Two-barrel cycle including loading is ~1.5 h. Residual oil in cake ≤7%.
Degumming with hot water + phosphoric acid for hydratable phospholipids, alkali neutralization to remove FFA, bleaching with activated earth, vacuum deodorization at 240–260 °C. The result is a pale yellow neutral oil suited to retail.
Machine ladder
Rapeseed model selection follows the variety-and-product decision: traditional flavor oil leans toward 300/325 hot press with light filtration; canola RBD leans toward 300/325 hot press plus a full refining train.
The variety must be identified at intake — they look similar but produce different oils. Traditional Brassica napus / Brassica juncea high-erucic varieties versus canola (Canadian-bred low-erucic, low-glucosinolate). This determines the entire downstream plan.
Steam-jacketed cooker conditions the seed before hydraulic pressing. Proper conditioning gives cleaner oil release, lower residual oil in cake, and the characteristic nutty aroma traditional buyers expect.
300 ton hot-press for moderate capacity, 325 ton for higher-pressure handling of stubborn seed batches. Two-barrel cycle including loading is ~1.5 h. Residual oil in cake ≤7%.
Degumming with hot water + phosphoric acid for hydratable phospholipids, alkali neutralization to remove FFA, bleaching with activated earth, vacuum deodorization at 240–260 °C. The result is a pale yellow neutral oil suited to retail.
Supporting equipment
Removes stones, metal, and stalk debris before flaking. Stones damage roller mills and contaminate cake. Magnetic separators are mandatory upstream of any pressing line for safety and equipment protection.
Flakes whole rapeseed to expose oil cells. Flake thickness directly controls hot-press yield. Under-flaking causes oil retention in cake; over-flaking generates fines that block press cloth.
Conditions flaked seed with steam. Adjusts moisture and temperature simultaneously. The cooker capacity must match daily press output — under-cooked feed reduces yield, over-cooked feed darkens the crude oil.
100 kg/barrel, 30–40 min per barrel, residual oil ≤7%. Two-barrel cycle ~1.5 h with loading. Robust, well-suited to year-round commercial operation. Cake discharges cleanly for feed milling.
Full RBD train using matching rapeseed refining section. Degumming reactor + neutralization tank + bleaching earth column + vacuum deodorizer. Output is pale yellow oil with FFA <0.05%, suitable for retail bottling.
Stainless storage tank for refined oil. Bottling line for 500 ml–5 L PET or glass for retail, plus 20 L drum-fill for foodservice. Traditional flavor oil may be packaged in dark glass to preserve aroma.
Project rhythm
Decision support
Keep the engineering path moving
Share feed condition, pretreatment depth, shift output, post-press destination, and utility limits. We use that to narrow the scope to the pressing section, clarification loop, and real factory boundary.