Homogenizing and/or dispersing device comprising endless screws

• US 7,025,491 B2
• Filed: 05/08/2002
• Issued: 04/11/2006
• Est. Priority Date: 05/09/2001
• Status: Expired due to Term

• Current Assignee: Blach Verwaltungs GmbH & Co., KG
• Original Assignee: 3+Extruder GmbH
• Inventors: Blach, Josef A., Blach, Markus, Blach, Michael
• Primary Examiner(s): SOOHOO, TONY GLEN
• Application Number:
  US10/477,442
• Publication Number:
  US 20040141405A1
• Time in Patent Office: 1,434 Days
• Field of Search: 366/83, 366/84, 366/85, 366/88, 425/204, 425/208, 425/209
• US Class Current: 366/85
• CPC Class Codes: B29B 7/485 with three or more shafts provided with screws
• CPC Class Codes: B29C 48/03 characterised by the shape of the extruded material at extrusion
• CPC Class Codes: B29C 48/43 Ring extruders
• CPC Class Codes: B29C 48/435 Sub-screws
• CPC Class Codes: B29C 48/44 Planetary screws
• CPC Class Codes: B29C 48/535 with thread pitch varying along the longitudinal axis

Abstract

An apparatus for homogenizing and/or dispersing at least one viscous substance and at least one solid and/or at least one other substance of different viscosity includes in a space in a housing axis-parallel rotatable shafts disposed along a circle with equal central-angle distance and provided with tightly intermeshing screw elements. The shafts in the area outside the openings in the housing are provided with screw elements having a pitch (S) of at most three quarters of the outside screw diameter (D) over a length (L=L1+L2+L3) corresponding to at least ten times the outside diameter (D) of the screw elements.

Claims

1. An apparatus for at least one of homogenizing and dispersing at least one viscous substance provided in combination with at least one solid or at least one other substance of different viscosity, having at least three axis-parallel rotatable shafts disposed in a screw space in a housing along a circle with equal central-angle distance and provided at least partly with tightly intermeshing screw elements, the housing being provided on the radially external and internal sides of the screw space with axis-parallel concave circular segments receiving the particular shaft and with openings into the screw space, wherein the shafts are provided in the area outside the openings over a length (L=L1+L2+L3) corresponding to at least ten times the outside screw diameter (D) of the screw elements with the screw elements having a pitch (S) of at most three quarters of the outside screw diameter (D) over a length of at least three times the outside diameter (D) of the screw elements.

2. The apparatus according to claim 1, wherein the pitch (S) is at most two thirds of the outside screw diameter (D).

3. The apparatus according to claim 1, wherein the screw elements are of single-flighted design.

4. The apparatus according to claim 3, wherein the flight width (K) of the screw elements is different in individual axial areas (M, N) at constant pitch (S).

5. The apparatus according to claim 1, wherein the screw elements have an elliptical contour in cross section, the curvature in the area of the major axis (A, B, A′

, B′

) corresponding to half the outside screw diameter (D) and in the area of the minor vertices (E, F, E′

, F′

) to the axial distance (Ax) of two said shafts minus half the outside screw diameter (D).

6. The apparatus according to claim 1, wherein said shafts are rotatable in the same direction.

7. The apparatus according to claim 1, wherein said apparatus is free from kneading blocks.

8. The apparatus according to claim 1, wherein said screw elements extend along the length of the entire portion of each said rotatable shaft that processes the viscous substance in combination with the at least one solid or the at least one other substance of different viscosity.

9. An apparatus for homogenizing and dispersing a viscous substance and at least one of solids and another viscous substance of different viscosity, comprising:

a cylindrical housing, including axial parallel concave circular segments defined by wedges therebetween, said cylindrical housing including a first opening at a first end for receiving the viscous substance and the at least one of solids and another viscous substance of different viscosity, and a second opening at a second output end;

an inside core in the housing including axis parallel concave circular segments defined by wedges therebetween, the inside core having the same number of corresponding axis parallel concave circular segments as the cylindrical housing, wherein the housing and inside core define an annular screw space; and

at least three axis-parallel rotatable shafts disposed in the annular screw space along a circle with equal central-angle distance, each said shaft received in corresponding ones of said concave circular segments of the housing and the inside core, the rotatable shafts being provided with tightly intermeshing screw elements having an outside screw diameter (D), the shafts having a length of at least ten times the outside screw diameter (D), the screw elements having a pitch (S) of at most three quarters of the outside screw diameter (D) over a length of at least three times the outside screw diameter (D),

wherein said rotatable shafts are rotated in the same direction and said apparatus is free of kneading blocks.

10. An apparatus according to claim 9, wherein the screw elements extend along the length of the entire portion of each said rotatable shaft that processes the viscous substance and the at least one of solids and another viscous substance of different viscosity.

11. An apparatus according to claim 9, wherein the screw elements have a pitch of at most one half of the outside screw diameter (D) and the screw elements extend along the entire length of each said rotatable shaft that processes the viscous substance and the at least one of solids and another viscous substance of different viscosity.

12. The apparatus according to claim 9, wherein the shafts have a length of at least fifteen times the outside screw diameter (D).

13. The apparatus of claim 9, wherein the screw elements are of single-flight design.

14. The apparatus according to claim 9, wherein the flight width of the screw elements is different in individual axial areas (M, N) having a constant pitch (S).

15. An apparatus for homogenizing and dispersing a viscous substance and at least one of solids and another viscous substance of different viscosity, comprising:

a cylindrical housing, including axial parallel concave segments defined by wedges therebetween, said cylindrical housing including a first opening at a first end for receiving the viscous substance and the at least one of solids and another viscous substance of different viscosity, and a second opening at a second output end;

an elongate inside core in the housing including axis parallel concave segments defined by wedges therebetween, the inside core having the same number of axis parallel concave segments as the cylindrical housing, wherein the housing and inside core define an annular screw space extending about the inside core; and

at least three axis-parallel rotatable shafts disposed in the annular screw space along a circle with equal central-angle distance, each said shaft received in corresponding ones of said concave circular segments of the housing and the inner core, the rotatable shafts being provided with tightly intermeshing screw elements having an outside screw diameter (D), the shafts having a length of at least ten times the outside screw diameter (D), the screw elements all having a pitch (S) of at most three quarters of the outside screw diameter (D), the screw elements extending along the length of the entire portion of each said rotatable shaft that processes the viscous substance and the at least one of solids and another viscous substance of different viscosity,

wherein said shafts are rotated in the same direction.

16. The apparatus according to claim 15, wherein said apparatus is free of kneading blocks.

17. The apparatus according to claim 16, wherein the screw elements are of single-flight design and have an elliptical contour in cross section, the curvature in the area of the major axis corresponding to half the outside screw diameter (D) and in the area of the minor vertices to the axial distance of two said shafts minus half the outside screw diameter (D).

18. The apparatus according to claim 16, wherein the flight width of the screw elements is different in individual axial areas (M, N) having a constant pitch (S).