Product and sterile transfer
Define viscosity, particles, filling temperature and sterile connection from the upstream sterilizer.
Manufacture and supply single-head aseptic filling machines for shelf-stable bag-in-drum filling of fruit puree, pulp, juice concentrate and sauce products.

Single-head aseptic filling machine for fruit puree, pulp and concentrate packaging.
For Single-Head Aseptic Filling Machine RFQ, provide product properties, package and spout, capacity and head count and sterilizer interface. These data are used to confirm the configuration, interfaces and quotation scope.
The position may vary according to finished product route, plant layout and sanitary design.
Control feed rate, inlet height and raw material condition before Single-Head Aseptic Filling Machine so the machine receives a stable load without bridging or unnecessary product damage.
Review this step with product data, line layout and sanitary requirements so Single-Head Aseptic Filling Machine can be integrated without creating a bottleneck.
Confirm outlet height, pump or conveyor interface, buffer need and next-machine inlet so the section connects cleanly to the production line.
Provide access for inspection, drain-down and cleaning so product-contact parts can be maintained without excessive downtime.
Review this step with product data, line layout and sanitary requirements so Single-Head Aseptic Filling Machine can be integrated without creating a bottleneck.
Single-Head Aseptic Filling Machine is commonly discussed for aseptic fruit puree, industrial pulp packaging, concentrate filling, bulk ingredient supply. The goal is to make this module work as part of a complete fruit and vegetable processing line, not as an isolated catalogue item.
Filling equipment is selected after the product route and thermal process are clear. Aseptic bag filling is used for shelf-stable bulk products after sterilization, while bottle, can or non-aseptic filling may require hot filling, pasteurization or refrigerated distribution depending on the product. Package size, cap or spout type, filling temperature, viscosity and particles directly affect filling head, measurement method and conveyor design.
For aseptic lines, CIP and SIP logic, sterile chamber design, spout sterilization, steam quality and sterile transfer from the UHT system must be reviewed together. For retail packaging, container rinsing, capping, labeling, date coding and tunnel pasteurization may become part of the scope. State whether the package is bag-in-drum, bag-in-box, bottle, can, jar or pouch, and mark all package sizes as reference until final supplier drawings are confirmed. The RFQ checklist below should be used to confirm the sizing data before quotation.
Related planning pages: tubular sterilizer before filling, double-head aseptic filling machine, and send an equipment RFQ. These internal links help compare equipment, plant route and RFQ scope before final quotation.
The questions below reflect the actual engineering inputs for this equipment category. Reference values are useful for early discussion, but final sizing is confirmed from project data and samples or drawings where needed.
Define viscosity, particles, filling temperature and sterile connection from the upstream sterilizer.
Confirm bag-in-drum or bag-in-bin format, bag volume, spout type, container handling and expected filling accuracy.
Plan steam quality, sterile chamber, spout sterilization, SIP sequence, head count and changeover time as one system.
Use this checklist when requesting a quote for Single-Head Aseptic Filling Machine. If values are preliminary, mark them as reference only so the engineering team can show adjustable options.
| RFQ Field | What to Provide | Why It Matters |
|---|---|---|
| Product properties | Product name, filling temperature, viscosity, Brix, pulp and maximum particle size. | Product behavior determines valve, filling path and measurement method. |
| Package and spout | Bag-in-drum or bag-in-bin, nominal volume, bag supplier, spout type and drum or bin dimensions. | Bag and spout details determine clamping, sterilization and container handling. |
| Capacity and head count | Required bags per hour, product flow, operating hours and changeover schedule. | Cycle time determines single- or double-head configuration and buffer needs. |
| Sterilizer interface | Upstream sterilizer type, sterile transfer pressure, pipe size, filling temperature and back-pressure requirement. | The filler and sterilizer must operate as one sterile section. |
| SIP, CIP and utilities | Steam pressure and quality, sterile air, compressed air, power, CIP connection, SIP sequence and condensate drainage. | Sterile utilities and cleaning logic determine aseptic reliability. |
The review checks where a single filling head fits the required sterile product flow, package size, change time, operator handling and upstream sterilizer capacity.
The page supports early project evaluation. Typical values are reference-only; final equipment selection requires product data, utility conditions and RFQ confirmation. Read our engineering content methodology.
Direct answers below explain the decisions that change process scope, equipment selection and quotation quality.
A single-head filler suits projects where required bag-in-drum or bag-in-bin throughput can be achieved with one filling station and acceptable package change time. It is often considered for moderate capacities or phased plants. Final selection must match package size, product flow, operator handling and the connected sterilizer output.
Real capacity includes sterile connection, bag handling, filling, disconnection and drum or bin movement. Product viscosity, foaming, target weight and operator rhythm also matter. Use packages per hour under defined product conditions, not only the filler inlet flow, because package change time can become the limiting part of the cycle.
Some designs can support different package sizes with suitable conveyors, supports, filling controls and bag interfaces, but this must be specified before manufacture. Drum and bin height, bag connection, target weight and movement method differ. A flexible requirement may add change parts, structure or control recipes that should appear clearly in the RFQ.
Provide viscosity and temperature at filling, Brix, fiber, particle type and maximum dimensions, target package weight and required flow. These values influence nozzle passage, valve selection, pressure drop and fill control. The upstream sterilizer and product pump must deliver the same validated product condition to the filler inlet.
Reserve floor space, conveyor alignment, sterile product header capacity, utilities, CIP flow, electrical load and PLC expansion. The upstream sterilizer should also have a realistic future capacity basis. Designing these interfaces during the first phase can reduce later shutdown and piping changes, even when the second filling head is not purchased immediately.
For a useful quotation, provide product properties, package and spout, capacity and head count and sterilizer interface. Mark preliminary values as reference only.