Determining production parameters of scale flow device

Claim 1

A method for determining process parameters of a production scale flow cell device, which comprises the steps of: a) effecting an emulsification to prepare a dispersed mixture by ultrasound using a device in a batchwise laboratory scale, and determining process parameters therefor; and b) effecting an emulsification to prepare a dispersed mixture by ultrasound in a continuous production scale with a flow cell by transferring directly there to the process parameters determined in step a), provided that a specific volume, dv/dt, is chosen for the flow cell which corresponds to an equivalent volume flow, dv eq /dt=vt, where v is a volume of a reaction chamber of a device, on a laboratory scale, and t is a sonication period; wherein said device comprises: a) a housing; and b) a reaction chamber within the housing and at least one sonotrode having a free emitting surface which is directly in effective connection with the reaction chamber and whose end remote from the free emitting surface is coupled to an ultrasonic transducer, wherein the sonotrode is designed as a rod-shaped, axially emitting longitudinal oscillator with said emitting surface corresponding essentially to the surface of the reaction chamber, and wherein the reaction chamber depth which is essentially vertical with respect to the emitting surface is lower than a maximum effective depth of the sonotrode.

Claim 2

A method for determining process parameters of a production scale flow cell device, which comprises the steps of: a) effecting an emulsification to prepare a dispersed mixture by ultrasound using a device in a batchwise laboratory scale, and determining process parameters therefor; and b) effecting an emulsification to prepare a dispersed mixture by ultrasound in a continuous production scale with a flow cell by transferring directly there to the process parameters determined in step a), provided that a specific volume, dv/dt, is chosen for the flow cell which corresponds to an equivalent volume flow, dv eq /dt=vt, where v is a volume of a reaction chamber of a device, on a laboratory scale, and t is a sonication period; wherein said device comprises: a) a housing; and b) a reaction chamber within the housing and at least one sonotrode having a free emitting surface which is directly in effective connection with the reaction chamber and whose end remote from the free emitting surface is coupled to an ultrasonic transducer, wherein the sonotrode is designed as a rod-shaped, axially emitting longitudinal oscillator with said emitting surface corresponding essentially to the surface of the reaction chamber, and wherein the reaction chamber depth which is essentially vertical with respect to the emitting surface is lower than a maximum effective depth of the sonotrode.

Claim 7

A method for determining process parameters of a production scale flow cell device, which comprises the steps of: a) effecting an emulsification to prepare a dispersed mixture by ultrasound using a device for producing disperse mixtures by means of ultrasound, in a batchwise laboratory scale, and determining process parameters therefor; and b) effecting an emulsification to prepare a dispersed mixture by ultrasound in a continuous production scale with a flow cell by transferring directly there to the process parameters determined in step a) wherein said device for producing disperse mixtures comprises a housing ( 11 ), a reaction chamber ( 12 ) within the housing and at least one sonotrode ( 13 ) having a free emitting surface ( 14 ) which is directly in effective connection with the reaction chamber ( 12 ) and whose end ( 18 ) remote from the free emitting surface is coupled to an ultrasonic transducer ( 19 ), wherein the sonotrode ( 13 ) is designed as a rod-shaped, axially emitting longitudinal oscillator with said emitting surface ( 14 ) corresponding essentially to the surface of the reaction chamber ( 12 ), and wherein the reaction chamber ( 12 ) depth ( 12 b ) which is essentially vertical with respect to the emitting surface ( 14 ) is lower than the maximum effective depth of the sonotrode ( 13 ).

Claim 8

A method for determining process parameters of a production scale flow cell device, which comprises the steps of: a) effecting an emulsification to prepare a dispersed mixture by ultrasound using a device for producing disperse mixtures by means of ultrasound, in a batchwise laboratory scale, and determining process parameters therefor; and b) effecting an emulsification to prepare a dispersed mixture by ultrasound in a continuous production scale with a flow cell by transferring directly there to the process parameters determined in step a) wherein said device for producing disperse mixtures comprises a housing ( 11 ), a reaction chamber ( 12 ) within the housing and at least one sonotrode ( 13 ) having a free emitting surface ( 14 ) which is directly in effective connection with the reaction chamber ( 12 ) and whose end ( 18 ) remote from the free emitting surface is coupled to an ultrasonic transducer ( 19 ), wherein the sonotrode ( 13 ) is designed as a rod-shaped, axially emitting longitudinal oscillator with said emitting surface ( 14 ) corresponding essentially to the surface of the reaction chamber ( 12 ), and wherein the reaction chamber ( 12 ) depth ( 12 b ) which is essentially vertical with respect to the emitting surface ( 14 ) is lower than the maximum effective depth of the sonotrode ( 13 ).

Claim 11

A method for determining process parameters of a production scale flow cell device, which comprises the steps of: a) effecting an emulsification to prepare a dispersed mixture by ultrasound using a device for producing disperse mixtures by means of ultrasound, in a batchwise laboratory scale, and determining process parameters therefor; and b) effecting an emulsification to prepare a dispersed mixture by ultrasound in a continuous production scale with a flow cell by transferring directly there to the process parameters determined in step a) wherein said device for producing disperse mixtures comprises a housing ( 11 ), a reaction chamber ( 12 ) within the housing which is arranged as a subsection of a through-flow reaction channel ( 15 ), and at least one sonotrode ( 13 ) having a free emitting surface ( 14 ) which is directly in effective connection with the reaction chamber ( 12 ) and whose end ( 18 ) remote from the free emitting surface is coupled to an ultrasonic transducer ( 19 ), wherein the sonotrode ( 13 ) is designed as a rod-shaped, axially emitting longitudinal oscillator with said emitting surface ( 14 ) of the sonotrode extending essentially over the entire width of the channel ( 15 ) and wherein the reaction chamber ( 12 ) depth ( 12 b ) which is essentially vertical with respect to the emitting surface ( 14 ) is lower than the maximum effective depth of the sonotrode ( 13 ).

Claim 12

A method for determining process parameters of a production scale flow cell device, which comprises the steps of: a) effecting an emulsification to prepare a dispersed mixture by ultrasound using a device for producing disperse mixtures by means of ultrasound, in a batchwise laboratory scale, and determining process parameters therefor; and b) effecting an emulsification to prepare a dispersed mixture by ultrasound in a continuous production scale with a flow cell by transferring directly there to the process parameters determined in step a) wherein said device for producing disperse mixtures comprises a housing ( 11 ), a reaction chamber ( 12 ) within the housing which is arranged as a subsection of a through-flow reaction channel ( 15 ), and at least one sonotrode ( 13 ) having a free emitting surface ( 14 ) which is directly in effective connection with the reaction chamber ( 12 ) and whose end ( 18 ) remote from the free emitting surface is coupled to an ultrasonic transducer ( 19 ), wherein the sonotrode ( 13 ) is designed as a rod-shaped, axially emitting longitudinal oscillator with said emitting surface ( 14 ) of the sonotrode extending essentially over the entire width of the channel ( 15 ) and wherein the reaction chamber ( 12 ) depth ( 12 b ) which is essentially vertical with respect to the emitting surface ( 14 ) is lower than the maximum effective depth of the sonotrode ( 13 ).