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Home/Applications/Synthetic biology/Continuous feeding
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Continuous feeding: flow-path protection

Application guide

This guide covers path protection in continuous feeding: component roles, action sequence, operating conditions and restart requirements. Identify the architecture before comparing configurations.

Application guides

Continuous feeding application guide

Continuous feeding fluidics overview
Syringe pumps in continuous feeding
Valveless Metering Pumps for Continuous Feeding
Supply mode
Fluidic valves in continuous feeding
Medium switching
Bubble and pressure sensing in continuous feeding
Fluidic Connections and Protection for Continuous Feeding
Flow-path protection

ON THIS PAGE

Where flow-path protection fits in the instrumentProduct responsibilities in this operationOrganize the sequence by actual architectureDefine operating conditions for this taskCompare product configurations by the roles on this pageValidate operation results at the receiverLocate abnormalities and restore the next operationReferencesRelated guides

01Where flow-path protection fits in the instrument

Configure protection for backpressure, check-valve cracking pressure, leakage and filter resistance. Validate backflow prevention and aseptic isolation separately, ensuring added resistance remains within the feed operating limits.

Check-valve opening pressure, filter pressure drop and backpressure affect the pump operating point. Backflow prevention and sterile isolation require separate validation.

02Product responsibilities in this operation

Tubing, fittings and the protection components described here form the actual path. Validate materials, passage dimensions, connection volume and maintenance state with this operation.

For this continuous feeding task, confirm check-valve cracking pressure, reverse leakage, filter pressure drop, actual load and maintenance state.

03Organize the sequence by actual architecture

  1. Identify locations requiring backflow restriction, culture-side backpressure and permitted flow direction. Check check-valve opening conditions and reverse-leakage requirements.
  2. Measure added resistance and actual feed flow in the installed configuration. If the path contains a filter, separately check its pressure drop and maintenance condition.
  3. Check backflow and output recovery after stopping, bottle changes and maintenance. Assess the full sterile boundary through tubing, fittings, vessels and cleaning or sterilization procedures.

04Define operating conditions for this task

Conditions, results and abnormality records for this operation
To defineDetails
Actual operating conditionsCheck-valve cracking pressure, reverse leakage, filter pressure drop, actual load and maintenance state
Acceptance targetMeasure opening load, normal flow, reverse leakage and recovery after replacement; validate sterile boundaries separately.
Fault localizationExcessive opening pressure, reverse leakage or filter blockage can disturb feeding.

05Compare product configurations by the roles on this page

Configuration options for the product roles on this page
ProductConfiguration optionConditions to verify
G-series check valvesBackflow limitationThe card shows a representative configuration. Confirm actual opening conditions, reverse leakage and medium separately.
Tubing materials and dimensionsConnection paths and shared volumeBore, length, load and actual formulation jointly determine materials and dimensions
Rigid-tubing fittingsTube-end positioning and sealed connectionsCheck tube outer diameter, threads, seal structure and port-bottom geometry
  • G-series check valves
  • Tubing materials and dimensions
  • Rigid-tubing fittings

06Validate operation results at the receiver

Measure opening load, normal flow, reverse leakage and recovery after replacement. Validate the sterile boundary separately.

Record output across the run, replenishment interruptions, first flow after bottle changes and reactor volume balance.

07Locate abnormalities and restore the next operation

Excessive opening pressure, reverse leakage or filter blockage can disturb feeding.

Preserve the current sample state first, then maintain the path and validate the new operating conditions.

Refilling or resetting a single syringe can interrupt supply. Continuous-operation capability and aseptic isolation both require system validation.

References

View references (3)
  1. [1]FOREACH G-series check valves: configurations and specifications
  2. [2]FOREACH tubing materials and dimensions: configurations and specifications
  3. [3]FOREACH rigid-tubing fittings: configurations and specifications

Related guides

  • Back to the continuous feeding fluidics overview
  • Fluidic Connections and Protection for Continuous Feeding

Related Products

G-series check valves; representative configuration. Select capacity, materials and interfaces for the application.

G-series check valves

Tubing materials and dimensions; representative configuration. Select capacity, materials and interfaces for the application.

Tubing materials and dimensions

Rigid-tubing fittings; representative configuration. Select capacity, materials and interfaces for the application.

Rigid-tubing fittings

Related Technical Articles

What is flow resistance calculation for? Using the Foreach calculator in fluid-path design and selection

The free flow rate of the pump meets the requirements. After installing the pipelines, valves and joints, the liquid supply at the end is insufficient. Flow resistance calculations can break the problem down into comparable data: what pressure differential is required at the target flow rate, where does the pressure loss mainly occur, and what happens if the pipe diameter, pipe length, component Cv or medium viscosity is changed. This article combines the actual function of the Foreach flow resistance calculator with a recalculable fluid circuit case to explain how to use the calculation results for design, selection, troubleshooting and prototype verification.

2026-09-11View Details

Why Does Actual Flow Change So Much When the Tubing Size Changes on the Same Miniature Diaphragm Pump?

Even when the pump is unchanged, installed flow can change because of tubing inner diameter, length, bends, and the minimum bore of fittings. When flow falls after a tubing change, the effective response is neither to blame the pump first nor to enlarge every tube indiscriminately. Measure inlet pressure, outlet pressure, and accumulated flow together to determine where the added restriction actually occurs.

2026-08-24View Details

Valveless Metering Pump Selection Guide: FOREACH Models and Applications

To select a valveless metering pump, first define the volume per dose and the time available for dispensing. Then check displacement per revolution, drive speed, wetted materials, backpressure and connections, and verify delivery in the actual fluid path. Neither flow rate alone nor the label ‘metering pump’ is enough to select a model.

2026-09-16View Details

Discuss fluidic configurations for continuous feeding

Provide a fluid diagram, the actual liquids and pressures in each state. Cards show representative configurations: confirm actual opening conditions, reverse leakage and medium separately; select tubing material and dimensions jointly for ID, length, load and actual formulation; and check tubing OD, threads, sealing structure and port-bottom geometry. Compare suitable configurations against the validation objectives described here.

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