U.S. patent application number 09/839507 was filed with the patent office on 2002-07-25 for high bulk paper.
This patent application is currently assigned to Consolidated Papers, Inc.. Invention is credited to Berger, Bernard J., Lau, Ralph L., Munce, Martin E..
Application Number | 20020096277 09/839507 |
Document ID | / |
Family ID | 25375404 |
Filed Date | 2002-07-25 |
United States Patent
Application |
20020096277 |
Kind Code |
A1 |
Lau, Ralph L. ; et
al. |
July 25, 2002 |
High bulk paper
Abstract
A method and apparatus are disclosed for making a high bulk,
coated paper of a unique structure with the coating forming a lower
portion of the total caliper and the paper base forming a higher
portion of the total caliper than conventionally made coated paper
of the same weight. The process includes the step of using furnish
with a high percentage of mechanical pulp, applying that furnish to
papermachine wires, preferably with a gap former, coating the paper
with a coating containing a plastic pigment, preferably of 4 or
more parts per 100 parts of coating pigment, and calendering the
coated paper at a nip loading less than conventional
supercalendering nip loading. Preferably, the finished coated paper
will have a 75.degree. TAPPI gloss of 40 or above. The method and
apparatus can be used to make lightweight or other weights of
coated paper.
Inventors: |
Lau, Ralph L.; (Port
Edwards, WI) ; Berger, Bernard J.; (Wisconsin Rapids,
WI) ; Munce, Martin E.; (Wisconsin Rapids,
WI) |
Correspondence
Address: |
PYLE & PIONTEK
221 N. LaSalle Street, Suite 850
Chicago
IL
60601
US
|
Assignee: |
Consolidated Papers, Inc.
|
Family ID: |
25375404 |
Appl. No.: |
09/839507 |
Filed: |
April 20, 2001 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
09839507 |
Apr 20, 2001 |
|
|
|
08880045 |
Jun 20, 1997 |
|
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|
Current U.S.
Class: |
162/136 ;
162/204; 162/205; 162/289; 162/361; 427/331 |
Current CPC
Class: |
D21H 11/10 20130101;
D21H 25/14 20130101; D21H 19/84 20130101; D21F 11/00 20130101; D21F
9/003 20130101; D21G 1/00 20130101; D21F 3/045 20130101; D21H 19/42
20130101; D21F 5/04 20130101 |
Class at
Publication: |
162/136 ;
162/205; 162/204; 162/361; 427/331; 162/289 |
International
Class: |
D21F 011/00; D21H
019/00 |
Claims
What is claimed is:
1. A papermaking apparatus for making a lightweight high bulk
coated paper web from a waterborne furnish containing at least 50%
mechanical pulp, comprising gap former section means for extruding
the furnish and forming the paper web from said furnish, press
section means for removing water from the formed paper web, dryer
means for drying the paper web to less than 10% moisture content,
coater means for applying a coating to the paper web, and means for
calendering the coated paper web to a finished caliper greater than
the caliper of conventional paper of the same weight and a
75.degree. TAPPI gloss of 40 or greater, whereby the coated paper
web formed is of high bulk in relation to its light weight with a
good gloss.
2. A papermaking apparatus as in claim 1, wherein said press
section means further comprises extended nip press means for
densifying the paper web less than would conventional press
means.
3. A papermaking apparatus as in claim 1, wherein said calender
means comprises hot-soft calender means for hot-soft calendering
the coated paper web.
4. A papermaking apparatus as in claim 1, wherein said calender
means comprises supercalender means for supercalendering the coated
paper web at a supercalender nip loading that is substantially less
than conventional supercalender nip loading.
5. A papermaking apparatus as in claim 1, wherein said coater means
comprises a blade coater for applying light coat weight to the
paper web.
6. A papermaking apparatus as in claim 5, wherein said blade coater
is a single blade coater.
7. A papermaking apparatus as in claim 5, wherein said blade coater
is a double blade coater.
8. A papermaking apparatus as in claim 6, wherein said blade coater
is a short dwell time applicator.
9. A papermaking apparatus as in claim 6, wherein said blade coater
is a fountain coater.
10. A papermalling apparatus as in claim 5, wherein said coater
includes a first blade coater with its own blade and a second blade
spaced downstream from said first blade coater.
11. A papermaking apparatus as in claim 10, wherein said first
blade coater is a short dwell time applicator.
12. A papermaking apparatus as in claim 5, further comprising a
second blade coater, the first blade coater operating on one side
of the paper web and the second blade coater operating on the other
side of the paper web.
13. A process for making lightweight high bulk coated paper
comprising the steps of: providing a waterborne furnish comprising
at least 50% mechanical pulp; forming a paper web by extruding the
furnish onto wire sides of a papermaking apparatus with a gap
former; pressing excess water from the paper web to provide a paper
web of a caliper that is substantially greater than that of a
conventional paper web of the same total weight; drying the paper
web to a moisture content of less than 10%; coating the paper web
with a coating weight that is substantially less than that applied
to conventional coated paper of the same total weight; and
calendering the coated paper web to a caliper greater than the
caliper of conventional coated paper of the same total weight, and
to a 75.degree. TAPPI gloss of 40 or greater; whereby a lightweight
coated paper is produced with a 75.degree. TAPPI gloss of at least
40 and with a greater paper base caliper and lesser coating caliper
than for conventional coated paper of the same total weight.
14. A process as in claim 13, wherein said pressing step includes
the step of densifying the paper web with an extended nip
press.
15. A process as in claim 13, wherein said calendering step
includes the step of hot-soft calendering the coated paper web.
16. A process as in claim 13, wherein said calendering step
includes the step of supercalendering the paper web at a
supercalender nip loading that is substantially less than nip
loading used in conventional supercalendering of conventional
coated paper of the same weight.
17. A process as in claim 16, wherein said supercalendering step is
carried out at a nip loading of about two-thirds of that for
conventional supercalendering of conventional coated paper of the
same weight.
18. A process as in claim 13, wherein the coated paper produced has
about 10 to 20% greater caliper than a conventional coated paper of
a same weight.
19. A process as in claim 13, wherein said step of forming the
paper web includes forming a base having a weight of about 24 to 34
pounds per ream.
20. A process as in claim 13, wherein said step of coating the
paper web includes applying a coat weight of 3 or less pounds per
ream on a side of the paper web.
21. A process as in claim 13, wherein said forming step includes
forming a base having a caliper of at least about 88% of the total
caliper of the finished coated paper.
22. A process as in claim 21, wherein said coating step includes
applying to a side of the web coating that is no more than about 6%
of the total caliper of the finished coated paper.
23. A process as in claim 21, wherein said coating step includes
applying to each of the two sides of the web coating that in total
is no more than about 12% of the total caliper of the finished
coated paper.
24. A process as in claim 23, wherein said coating step includes
applying to the paper web a coating that is not in excess of about
12% of the total caliper of the finished coated paper.
25. A process as in claim 24, wherein said coating step includes
applying about one-half of the coating to each side of the paper
web.
26. A process as in claim 24, wherein said forming step provides
the balance of the percentage of the total caliper of the finished
coated paper.
27. A process as in claim 13, wherein said coating step includes
coating the paper web with a coating containing plastic
pigment.
28. A process as in claim 27, wherein said calendering step
includes calendering the paper to a 75.degree. TAPPI gloss of at
least 40.
29. A process as in claim 13, where said step of coating the paper
web includes applying coating having a weight of about 4 to 6
pounds per ream.
30. A process as in claim 13, wherein said steps of forming and
coating include forming a base that comprises about 75 to 85% by
weight of the total weight of the coated paper and applying a
coating to the base that comprises about 25 to 15% by weight of the
total weight of the coated paper.
31. A process as in claim 30, wherein said forming and coating
steps include forming a base that comprises about 80 to 85% by
weight, and applying a coating to the base that comprises about 20
to 15% by weight, of the total weight of the coated paper.
32. A lightweight high bulk coated paper with a 75.degree. TAPPI
gloss of at least 40, comprising a paper base of a weight of 24 to
34 pounds per ream, a coating containing a plastic pigment on each
side of said base, said coating being of a weight of no more than 3
pounds per ream per side, said base having a caliper of at least
about 88% of the total caliper of said coated paper and said
coating providing substantially the remainder of said caliper of
said coated paper, said coated paper having a 75.degree. TAPPI
gloss of at least 40.
33. A paper as in claim 32, wherein said plastic pigment of said
coating is at least 4 parts per 100 parts pigment of said
coating.
34. A paper as in claim 32, wherein said base comprises about 75 to
85% by weight, and said coating comprises about 25 to 15% by
weight, of the total weight of said coated paper.
35. A paper as in claim 32, wherein said coating weight on at least
one side of said web comprises about 1.5 to 3 pounds per ream.
36. A paper as in claim 32, wherein said coating is applied in
substantially equal weights on each side of said base.
37. A paper as in claim 32, wherein base comprises at least 55%
mechanical pulp.
38. A paper as in claim 32, wherein said base is a gap formed
base.
39. A paper as in claim 32, wherein said base is an extended nip
pressed base.
40. A paper as in claim 32, wherein said coated paper is a
supercalendered coated paper having a 75.degree. TAPPI gloss of at
least 40.
41. A paper as in claim 32, wherein said coated paper is a coated
paper that has been supercalendered at about two-thirds
conventional supercalendering nip loads.
42. A paper as in claim 32, wherein said coated paper is a hot-soft
calendered coated paper having a 75.degree. TAPPI gloss of at least
40.
43. A paper as in claim 32, wherein said coated paper has a
75.degree. TAPPI gloss of at least 45.
44. A paper as in claim 32, wherein said coated paper is a coated
paper that has been calendered to a 75.degree. TAPPI gloss of at
least 45.
45. A papermaking apparatus for making an ultralightweight high
bulk coated paper web from a waterborne furnish containing at least
50% mechanical pulp, comprising gap former section means for
extruding the furnish and forming the paper web from said furnish,
press section means for removing water from the formed paper web,
dryer means for drying the paper web to less than 10% moisture
content, coater means for applying a coating to the paper web, and
means for calendering the coated paper web to a finished caliper
greater than the caliper of conventional paper of the same weight
and to a 75.degree. TAPPI gloss of 35, whereby the coated paper web
formed is of high bulk in relation to its ultralightweight with a
good gloss for its weight.
46. A papermaking apparatus as in claim 45, wherein said press
section means further comprises wide nip press means for densifying
the paper web less than would conventional press means.
47. A papermaking apparatus as in claim 45, wherein said calender
means comprises hot-soft calender means for hot-soft calendering
the coated paper web.
48. A papermaking apparatus as in claim 45, wherein said calender
means comprises supercalender means for supercalendering the coated
paper web at a supercalender nip loading that is substantially less
than conventional supercalender nip loading.
49. A papermaking apparatus as in claim 45, wherein said coater
means comprises a blade coater for applying light coat weight to
the paper web.
50. A papermaking apparatus as in claim 49, wherein said blade
coater is a single blade coater.
51. A papermaking apparatus as in claim 49, wherein said blade
coater is a double blade coater.
52. A papermaking apparatus as in claim 50, wherein said blade
coater is a short dwell time applicator.
53. A papermaking apparatus as in claim 50, wherein said blade
coater is a fountain coater.
54. A papermaking apparatus as in claim 49, wherein said coater
includes a first blade coater with its own blade and a second blade
spaced downstream from said first blade coater.
55. A papermaking apparatus as in claim 54, wherein said first
blade coater is a short dwell time applicator.
56. A papermaking apparatus as in claim 49, further comprising a
second blade coater, the first blade coater operating on one side
of the paper web and the second blade coater operating on the other
side of the paper web.
57. A process for making ultralightweight high bulk coated paper
comprising the steps of: providing a waterborne furnish comprising
at least 50% mechanical pulp; forming a paper web by extruding the
furnish onto wire sides of a papermaking apparatus with a gap
former; pressing excess water from the paper web to provide a paper
web of a caliper that is substantially greater than that of a
conventional paper web of the same total weight; drying the paper
web to a moisture content of less than 10%; coating the paper web
with a coating weight that is substantially less than that applied
to conventional coated paper of the same total weight; and
calendering the coated paper web to a caliper greater than the
caliper of conventional coated paper of the same total weight, and
to a 75.degree. TAPPI gloss of at least 35. whereby an
ultralightweight coated paper is produced with a 75.degree. TAPPI
gloss of at least 35 and with a greater paper base caliper and
lesser coating caliper than for conventional coated paper of the
same total weight.
58. A process as in claim 57, wherein said pressing step includes
the step of densifying the paper web with an extended nip
press.
59. A process as in claim 57, wherein said calendering step
includes the step of hot-soft calendering the coated paper web.
60. A process as in claim 57, wherein said calendering step
includes the step of supercalendering the paper web at a
supercalender nip loading that is substantially less than nip
loading used in conventional supercalendering of conventional
coated paper of the same weight.
61. A process as in claim 60, wherein said supercalendering step is
carried out at a nip loading of about two-thirds of that for
conventional supercalendering of conventional coated paper of the
same weight.
62. A process as in claim 57, wherein the coated paper produced has
about 10 to 20% greater caliper than a conventional coated paper of
a same weight.
63. A process as in claim 57, wherein said step of forming the
paper web includes forming a base having a weight of about 18 to
less than 24 pounds per ream.
64. A process as in claim 57, wherein said step of coating the
paper web includes applying a coat weight of 2 or less pounds per
ream on a side of the paper web.
65. A process as in claim 57, wherein said forming step includes
forming a base having a caliper of at least about 88% of the total
caliper of the finished coated paper.
66. A process as in claim 65, wherein said coating step includes
applying to a side of the web coating that is no more than about 6%
of the total caliper of the finished coated paper.
67. A process as in claim 65, wherein said coating step includes
applying to each of the two sides of the web coating that in total
is no more than about 12% of the total caliper of the finished
coated paper.
68. A process as in claim 57, wherein said coating step includes
applying to the paper web a coating that is not in excess of about
12% of the total caliper of the finished coated paper.
69. A process as in claim 68, wherein said coating step includes
applying about one-half of the coating to each side of the paper
web.
70. A process as in claim 68, wherein said forming step provides
the balance of the percentage of the total caliper of the finished
coated paper.
71. A process as in claim 57, wherein said coating step includes
coating the paper web with a coating containing plastic
pigment.
72. A process as in claim 61, wherein said calendering step
includes calendering the paper to a 75.degree. TAPPI gloss of at
least 35.
73. A process as in claim 57, where said step of coating the paper
web includes applying coating having a weight of about 18 to less
than 24 pounds per ream.
74. A process as in claim 57, wherein said steps of forming and
coating include forming a base that comprises about 75 to 85% by
weight of the total weight of the coated paper and applying a
coating to the base that comprises about 25 to 15% by weight of the
total weight of the coated paper.
75. A process as in claim 57, wherein said forming and coating
steps include forming a base that comprises about 80 to 85% by
weight, and applying a coating to the base that comprises about 20
to 15% by weight, of the total weight of the coated paper.
76. An ultralightweight high bulk coated paper with a 75.degree.
TAPPI gloss of at least 35, comprising a paper base of a weight of
18 to less than 24 pounds per ream, a coating containing a plastic
pigment on each side of said base, said coating being of a weight
of no more than 2 pounds per ream per side, said base having a
caliper of at least about 88% of the total caliper of said coated
paper and said coating providing substantially the remainder of
said caliper of said coated paper, said coated paper having a
75.degree. TAPPI gloss of at least 35.
77. A paper as in claim 76, wherein said plastic pigment of said
coating is at least 4 parts per 100 parts pigment of said
coating.
78. A paper as in claim 76, wherein said base comprises about 75 to
85% by weight, and said coating comprises about 25 to 15% by
weight, of the total weight of said coated paper.
79. A paper as in claim 76, wherein said coating weight on at least
one side of said web comprises about 1.0 to 2.0 pounds per
ream.
80. A paper as in claim 76, wherein said coating is applied in
substantially equal weights on each side of said base.
81. A paper as in claim 76, wherein base comprises at least 55%
mechanical pulp.
82. A paper as in claim 76, wherein said base is a gap formed
base.
83. A paper as in claim 76, wherein said coater paper is a
supercalendered coated paper having a 75.degree. TAPPI gloss of at
least 35.
84. A paper as in claim 76, wherein said coated paper is a coated
paper that has been supercalendered at about two-thirds
conventional supercalendering nip loads.
85. A paper as in claim 76, wherein said coated paper is a hot-soft
calendered coated paper having a 75.degree. TAPPI gloss of at least
35.
86. A paper as in claim 76, wherein said coated paper has a
75.degree. TAPPI gloss of at least 40.
87. A paper as in claim 76, wherein said coated paper is a coated
paper that has been calendered to a 75.degree. TAPPI gloss of at
least 40.
88. A papermaking apparatus for making high bulk coated paper web
from a waterborne furnish containing at least 50% mechanical pulp,
comprising double wire former section means for extruding the
furnish and forming the paper web from said furnish, extended nip
press section means for removing water from the formed paper web,
dryer means for drying the paper web to less than 10% moisture
content, coater means for applying a coating to the paper web, and
means for hot-soft calendering the coated paper web to a finished
caliper greater than the caliper of conventional paper of the same
weight and to a 75.degree. TAPPI gloss of 40 or greater, whereby
the coated paper web formed is of high bulk in relation to its
light weight with a good gloss.
89. A papermaking apparatus as in claim 88, wherein said coater
means comprises a blade coater for applying light coat weight to
the paper web.
90. A papermaking apparatus as in claim 89, wherein said blade
coater is a single blade coater.
91. A papermaking apparatus as in claim 89, wherein said blade
coater is a double blade coater.
92. A papermaking apparatus as in claim 90, wherein said blade
coater is a short dwell time applicator.
93. A papermaking apparatus as in claim 90, wherein said blade
coater is a fountain coater.
94. A papermaking apparatus as in claim 89, wherein said coater
includes a first blade coater with its own blade and a second blade
spaced downstream from said first blade coater.
95. A papermaking apparatus as in claim 94, wherein said first
blade coater is a short dwell time applicator.
96. A papermaking apparatus as in claim 89, further comprising a
second blade coater, the first blade coater operating on one side
of the paper web and the second blade coater operating on the other
side of the paper web.
97. A process for making high bulk coated paper comprising the
steps of: providing a waterborne furnish comprising at least 50%
mechanical pulp; forming a paper web by extruding the furnish onto
wire sides of a papermaking apparatus with a double wire former;
pressing excess water from the paper web with an extended nip press
to provide a paper web of a caliper that is substantially greater
than that of a conventional paper web of the same total weight;
drying the paper web to a moisture content of less than 10%;
coating the paper web with a coating weight that is substantially
less than that applied to conventional coated paper of the same
total weight; and hot-soft calendering the coated paper web to a
caliper greater than the caliper of conventional coated paper of
the same total weight, and to a 75.degree. TAPPI gloss of at least
40; whereby a coated paper is produced with a 75.degree. TAPPI
gloss of at least 40 and with a greater paper base caliper and
lesser coating caliper than for conventional coated paper of the
same total weight.
98. A process as in claim 97, wherein the coated paper produced has
about 10 to 20% greater caliper than a conventional coated paper of
a same weight.
99. A process as in claim 97, wherein said step of forming the
paper web includes forming a base having a weight of about 18 to 40
pounds per ream.
100. A process as in claim 97, wherein said step of coating the
paper web includes applying a coat weight of 3 or less pounds per
ream on a side of the paper web.
101. A process as in claim 97, wherein said forming step includes
forming a base having a caliper of at least about 88% of the total
caliper of the finished coated paper.
102. A process as in claim 101, wherein said coating step includes
applying to a side of the web coating that is no more than about 6%
of the total caliper of the finished coated paper.
103. A process as in claim 97, wherein said coating step includes
applying about one-half of the coating to each side of the paper
web.
104. A process as in claim 97, wherein said coating step includes
coating the paper web with a coating containing plastic
pigment.
105. A process as in claim 97, where said step of forming the paper
web includes forming a base having a weight of about 18 to 34
pounds per ream.
106. A process as in claim 97, wherein said steps of forming and
coating include forming a base that comprises about 75 to 85% by
weight of the total weight of the coated paper and applying a
coating to the base that comprises about 25 to 15% by weight of the
total weight of the coated paper.
107. A process as in claim 97, wherein said forming and coating
steps include forming a base that comprises about 80 to 85% by
weight, and applying a coating to the base that comprises about 20
to 15% by weight, of the total weight of the coated paper.
108. A high bulk coated paper with a 75.degree. TAPPI gloss of at
least 40, comprising a paper base of a weight of 18 to 34 pounds
per ream, a coating containing a plastic pigment on each side of
said base, said coating being of a weight of no more than 3 pounds
per ream per side, said base having a caliper of at least about 88%
of the total caliper of said coated paper and said coating
providing substantially the remainder of said caliper of said
coated paper, said coated paper having a 75.degree. TAPPI gloss of
at least 40.
109. A paper as in claim 108, wherein said plastic pigment of said
coating is at least 4 parts per 100 parts pigment of said
coating.
110. A paper as in claim 108, wherein said base comprises about 75
to 85% by weight, and said coating comprises about 25 to 15% by
weight, of the total weight of said finished coated paper.
111. A paper as in claim 108, wherein said coating weight on at
least one side of said web comprises about 1.0 to 3 pounds per
ream.
112. A paper as in claim 111, wherein said coating is applied in
substantially equal weights on each side of said base.
113. A paper as in claim 108, wherein base comprises at least 55%
mechanical pulp.
114. A paper as in claim 108, wherein said coated paper has a
75.degree. TAPPI gloss of at least 40.
115. A paper as in claim 108, wherein said coated paper is a coated
paper that has been calendered to a 75.degree. TAPPI gloss of at
least 45.
Description
DISCLOSURE
[0001] This invention relates to high bulk paper and preferably to
high bulk coated paper with good printed gloss.
BACKGROUND OF THE INVENTION
[0002] Heretofore, it has been known to make lightweight, high bulk
paper. For example, see U.S. Pat. No. 5,283,129, the teachings of
which are incorporated herein by reference. However, that patent
achieves high bulk by using coating that tends to be bulkier than
conventional coating.
[0003] Other prior art attempts have been used to make high bulk
coated paper by utilizing lower than conventional supercalendering
nip pressures. However, these papers generally had low gloss,
usually well below a 75.degree. TAPPI gloss of 40, namely about 35.
Consolidated Papers, Inc., the assignee of the present invention,
had commercially sold similarly made lower gloss, high bulk papers
as early as 1993. Such lower gloss paper is not acceptable for many
publication purposes, such as magazines where lightweight, high
bulk paper, with high gloss and good print gloss has been desired
and sought for years due to ever increasing mailing rates.
BRIEF SUMMARY OF THE INVENTION
[0004] A method and apparatus is disclosed for making a high bulk,
coated paper of a unique structure with the coating forming a lower
portion of the total caliper and the paper base forming a higher
portion of the total caliper than conventionally made coated paper
of the same weight. This approach provides a bulkier, coated paper.
The process includes the steps of using furnish with a high
percentage, say over 50%, and preferably in a range of 55 to 75%,
with a target of 60 to 65%, of mechanical pulp, or other similar
pulps described herein, applying that furnish to two or twin wire
papermachines, preferably with a gap former, coating the paper with
a coating containing a plastic pigment in a concentration of 4 or
more parts, and preferably 7 or more parts per 100 parts of coating
pigment, and calendering the coated paper at a loading less than
conventional supercalender loading. The use of mechanical pulp in
the base sheet and a high content of plastic pigment in the coating
gives a good surface finish that is easily calendered, either by
lower pounds per linear inch supercalendering or hot-soft
calendering to a high gloss acceptable to most publishers
interested in lightweight coated paper for magazines or other
similar uses. Preferably, the finished coated paper will have a
75.degree. TAPPI gloss of 40 or above. The method or process and
apparatus of the present invention can also be used to make other
than lightweight grades of coated paper such as ultra lightweight
coated paper. While the invention is directed toward coated paper
for offset printing, it can be utilized for other coated papers for
gravure, flexographic or letterpress printing.
BRIEF DESCRIPTION OF THE DRAWINGS
[0005] The present invention method, apparatus and paper itself is
described in conjunction with the following drawings wherein:
[0006] FIG. 1 shows a gap former section for use with the present
invention;
[0007] FIG. 2A shows a conventional press section;
[0008] FIG. 2B shows an extended nip press section for use with the
present invention;
[0009] FIG. 2C shows another version of an extended nip press for
use with the present invention;
[0010] FIG. 3 shows a main dryer section for use with the present
invention, which connects to FIG. 4 as shown by the heavy
arrows;
[0011] FIG. 4 shows two online coaters and accompanying coater
dryers for use with the present invention;
[0012] FIG. 5A shows tandem hot-soft calenders for use with the
present invention;
[0013] FIG. 5B shows a supercalender for use with the present
invention;
[0014] FIG. 6A shows conventional prior art lightweight coated
paper of the same weight as in FIGS. 6B to 6D;
[0015] FIG. 6B shows prior art Consolidated Papers, Inc. made
coated paper;
[0016] FIG. 6C shows other prior art coated paper; and
[0017] FIG. 6D shows coated paper of the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0018] As briefly discussed above, publishers and printers
generally desire paper with gloss in unprinted portions and high
print gloss with good ink/color properties in printed portions.
Attempts have been ongoing to develop high bulk, lightweight coated
papers with high print gloss.
[0019] In the present invention, a high bulk coated paper is
developed which proportionally uses more base stock and less coat
weight than similar grades of conventional paper of the same total
weight. For example, while a conventional 30 pounds per ream paper,
where herein a ream is 3300 square feet of paper, may have the
following properties:
1 Base Weight Coating Weight 22 lbs./rm 8 lbs./rm
[0020] paper of the present invention has:
2 Base Weight Coating Weight 25 lbs./rm 5 lbs./rm
[0021] For a heavier paper of 32 lbs. per ream the data is:
3 Conventional Present Invention Base Weight Coating Weight Base
Weight Coating Weight 24 lbs./rm 8 lbs./rm 26.5 lbs./rm 5.5
lbs./rm
[0022] For 38 pound paper:
4 Conventional Present Invention Base Weight Coating Weight Base
Weight Coating Weight 27 lbs./rm 11 lbs./rm 31.5 lbs./rm 6.5
lbs./rm
[0023] The caliper of the papers above are as follows:
5 Caliper Caliper Pound Conventional Present Invention 30 1.5 to
1.65 mils 1.75 to 1.9 mils 32 1.6 to 1.75 mils 1.85 to 2.0 mils 38
1.8 to 2.0 mils 2.0 to 2.2 mils
[0024] The paper of the present invention, made using the method
and apparatus of the present invention, would start with a
waterbome furnish having a high percentage of mechanical pulp,
generally in excess of 50%, usually in the 55 to 75% range, and
preferably about 65%. Mechanical pulp gives a well formed base. As
used herein, the term mechanical pulp may include stone ground wood
(SGW), pressurized ground wood (PGW) and chemi ground wood (CGW),
refiner mechanical pulp (RMP), thermal mechanical pulp (TMP), and
chemi thermal mechanical pulp (CTMP). Sample furnish formulations
are: (1) 45% TMP/20% SGW/35% softwood Kraft (SWK) and (2) 50%
TMP/25% PGW/25% SWK. SWK is not considered a mechanical pulp.
Another example might be 70-85% CTMP/30-15% SWK.
[0025] The furnish preferably is utilized in a papermaking
apparatus or machine having a gap former (FIG. 1) instead of a
conventional fourdinier. A typical gap former for use with the
present invention is a Voith-Sulzer GmbH Duo Former CFD. The gap
former provides somewhat denser web base surfaces so that an AVS
formation index of 75% or greater with a flock index of 15 or less
and a void index of 15 or less are achieved, providing a smooth,
more uniform base paper which is more easily covered with less coat
weight as discussed below. The less porous paper surface reduces or
minimizes coating penetration. The inherent ability of former gap
to reduce two sidedness of the paper base permits achieving minimum
coating application with good gloss.
[0026] The above made paper then moves into the press section
wherein it can be conventionally pressed. Preferably, the press
section may include a wide shoe or extended nip press (FIG. 2B or
2C) which is believed will compress the web less than is
conventional, resulting in the paper web retaining more bulk and/or
caliper. The extended nip press preserves bulk, yet permits water
removal from the web due to the extended time the web is in the
nip, which permits use of a nip pressure that is lower than
conventional. Such an extended nip press is made by Beloit
Corporation as model ENP-C.
[0027] The web is then sent through the dryer section (FIG. 3) and
dried to a moisture content of below 10%, and preferably to 5% or
less. The paper may then be coated on or off the papermaking
machine.
[0028] As noted above, the coating weight applied to the web is
less than conventional, but because of the smoothness and
uniformity of the gap formed paper base, the paper base can be
acceptably coated with a lesser amount of coating, thus yielding
high bulk and allowing a given weight paper to proportionally
comprise a greater percentage of paper base and a lesser percentage
of coating than is conventional. Additionally, to provide increased
stiffness and good gloss, the coating contains a small percentage
of plastic pigment, advantageously at least 4% and preferably over
7%, and up to 20%. The amount of plastic pigment used can be
increased to compensate for the use of lower amounts of mechanical
pulp. Plastic pigment is relatively expensive, presently over one
dollar a pound. The pigments used may be, for example, #2 clay,
delaminated clay, calcined clay, TiO.sub.2 and plastic pigment. The
coating is generally, but need not be, applied to both sides of the
paper web. A sample pigment formulation is 89% delaminated clay, 4%
TiO.sub.2, and 7% HSP 1055 plastic pigment made by Rohm Haas. This
pigment can be made up into a typical coating with the addition of
other materials as may include starch, polymeric latex binders and
additives as shown below:
6 Parts by Material Weight B.D. Pigments: Delaminated Clay 88
TiO.sub.2 5 HSP 1055 (Plastic Pigment) 7 Dispersant: Sodium
Polyacrylate 0.1 Binders: Starch 5 SBR Latex 11 Lubricant:
Diglyceride 0.9 Water -- % Solids 53%
[0029] Generally, the coating can be applied with any conventional
type blade coater and preferably with a short dwell time applicator
as shown in U.S. Pat. Nos. 4,250,211 and 4,512,279 (FIG. 4), and/or
a fountain type coater shown in U.S. Pat. No. 5,436,030 and/or a
double bladed coater as shown in U.S. Pat. No. 5,112,653, the
teachings of which patents are incorporated herein by reference. In
addition, the coating can be applied by a film coater or
Speedcoater applicator made by Voith Sulzer GmbH, such as that
shown in U.S. Pat. No. 4,848,268. While blade doctoring is
preferred, other suitable types of metering, such as with a doctor
rod, grooved or smooth, could be used. The term blade or blade
coater as used herein, unless specifically stated, is understood to
include such other equivalent metering techniques. The doctor blade
shown in U.S. Pat. No. 4,780,336 has been advantageously used to
provide low coat weight.
[0030] The coated paper can then be calendered, preferably hot-soft
calendered (FIG. 5A) and/or supercalendered (FIG. 5B), but for
supercalendering the nip pressure is less than normal. The hot-soft
calendering provide some improvement in bulk over supercalendering
at a lower nip pressure. This improvement could be about 5 to 7%
greater bulk. For example, a reduced supercalendering nip load
gives a bulk factor of 58, while hot-soft calendering on the same
coater paper stock at equal gloss (42) gives a bulk factor of 61.
Supercalendering equipment useful in the present invention is a 10
nip supercalender made by Voith Sulzer GmbH. When used to
supercalender the coated paper of the invention, the nips of the
supercalender would be at a loading of only about two-thirds (2/3)
of what is conventionally used. For example, supercalender loading
may be 800 to 1200 pounds (per lineal inch) with 1100 to 1200
pounds being preferred and about 1150 pounds being the target,
instead of the usual 1500 to 2200 pounds. Hot-soft calendering can
be carried out under conventional conditions and may also take
place on or off the machine. Hot-soft calendering equipment such as
shown in U.S. Pat. Nos. 3,124,480, 3,124,504, 3,230,867 or
4,277,524 and/or currently made and offered by Voith Sulzer GmbH as
Model No. G30 2/0 may be used. Generally, but not necessarily,
supercalendering will take place off machine. However, if apparatus
similar to the Janus calender made by Voith-Sulzer GmbH is used,
such low nip load calendering could be performed on-line.
[0031] The resultant coated paper will generally have a bulk factor
of 57-62% which can be expressed as a function of its total weight
as follows: 1 Caliper in mils .times. 1000 Base weight per ream
[0032] The resultant coated paper will generally have the following
characteristics as compared to conventional coated paper of the
same weight:
[0033] (1) 10-20% less lineal feet/roll of paper for the same roll
diameter, evidencing the higher bulk of the paper;
[0034] (2) lesser weight per roll for the same roll diameter;
[0035] (3) about 10-20% higher caliper;
[0036] (4) about 10-15% higher stiffness;
[0037] (5) about 0.5 to 1.0 pt. or more gain in opacity and
brightness; and
[0038] (6) print smoothness and gloss equivalent to conventional
paper.
[0039] Some of the parameters contemplated for, and for the making
of, the high bulk lightweight coated paper of the invention
are:
7 Basis Weight 32 30 28 26 24 Base Paper Weight 26-28 24-26 22-24
20-22 18-20 Coating Weight 4-6 4-6 4-6 4-6 4-6 Furnish Composition
% MP 55-75 55-75 55-75 55-75 55-75 % SW Kraft 25-45 25-45 25-45
25-45 25-45 % Ash 4-8 4-8 4-8 4-8 4-8 Coating Formula Part DL Clay
85 .+-. 7 85 .+-. 7 85 .+-. 7 85 .+-. 7 85 .+-. 7 Part TiO.sub.2 8
.+-. 4 8 .+-. 4 8 .+-. 4 8 .+-. 4 8 .+-. 4 Part Plastic Pigment 7
.+-. 3 7 .+-. 3 7 .+-. 3 7 .+-. 3 7 .+-. 3 Part Starch 3 .+-. 3 3
.+-. 3 3 .+-. 3 3 .+-. 3 3 .+-. 3 Part Latex 12 .+-. 3 12 .+-. 3 12
.+-. 3 12 .+-. 3 12 .+-. 3 Base Paper Kajaani Formation 65-100
65-100 65-100 65-100 65-100 Supercalender # Nips/side 1-5 1-5 1-5
1-5 1-5 Nip load - pli 1000-1400 1000-1400 1000-1400 1000-1400
1000-1400 Roll Temperature .degree. F. 16-225 160-225 160-225
160-225 160-225
[0040] While mechanical pulp is preferable, it is contemplated that
other pulps could be included, such that a lower percentage of
mechanical pulp would be required. Other pulps and proportions
thereof contemplated for use are as follows:
8 Percentage of Type of Other Percentage of Other Mechanical Pulp
Pulp Pulp A. 65% SWK 35% B. 60% SWK/HWK 30%/10% C. 60% SWK/recycled
30%/10%
[0041] While it is preferable to use a gap former, other types of
formers, such as twin wire or top wire formers, could instead be
used with some small sacrifice in bulk.
[0042] For example, several or many of the above discussed factors
could be used in combination to produce high bulk paper.
[0043] Factors effecting high bulk are listed as follows in
decreasing order of effectiveness:
[0044] 1. Low supercalender nip load or hot-soft calender;
[0045] 2. Gap former;
[0046] 3. Low coat weight/high substrate weight;
[0047] 4. Plastic pigment in coating;
[0048] 5. High % mechanical pulp;
[0049] 6. High latex/starch ratio binder; and
[0050] 7. Extended nip press (uncertain of the effect at the time
of filing).
[0051] Combinations of factors affecting the production of high
bulk paper as contemplated by the invention include (1) mechanical
pulp, two wire forming, decreased base weight, increased coat
weight, plastic pigment, and hot-soft calendering; (2) mechanical
pulp, gap forming, increased base weight, decreased coat weight,
plastic pigment coating, and supercalendering to a lower loading;
(3) mechanical pulp, decreased base weight, two wire forming,
extended nip or extended shoe pressing, uncured coat weight,
plastic pigment coating, and hot-soft calendering or
supercalendering to a lower load.
[0052] For example, the combination of:
[0053] 1. increasing base substrate weight from 24#/3300 ft.sup.2
to 26#/3300 ft.sup.2;
[0054] 2. increasing mechanical pulp in the base subtract from 52%
to 65%;
[0055] 3. decreasing coat weight from 8#/3300 ft.sup.2 to 6#/3300
ft.sup.2;
[0056] 4. decreasing supercalendering intensity from 1500 pli to
1150 pli; and
[0057] 5. increasing plastic pigment in the coating from 0 parts to
7 parts would increase bulk from 51.+-.1 to 58.+-.1 and increase
L&W stiffness from 42.+-.5 to 50.+-.5.
[0058] Conventional 32#, Conventional 34# and High Bulk 32# are
compared as follows:
9 Conventional Conventional High Bulk Basis Weight #/3,300 ft.sup.2
32 34 32 Base Substrate Weight #/ 24 251/2 26 3,300 ft.sup.2 Coat
Weight #/3,300 ft.sup.2 8 81/2 6 Caliper 1.62 .+-. .04 1.80 .+-.
.04 1.85 .+-. .04 Bulk Factor 51 .+-. 1 52 .+-. 1 58 .+-. 1 L&W
Stiffness 42 .+-. 5 55 .+-. 5 60 .+-. 5
[0059] The invention provides a high bulk lightweight coated paper
that is desirable for use in magazines which require very low basis
weight to reduce paper costs by increasing printing area per ton of
paper and by reducing mailing cost per magazine. High bulk paper
will improve the economics of publishing magazines by allowing a
lower basis weight to be substituted for a higher basis weight
conventional grade.
[0060] In addition, the increased stiffness of the paper of the
invention improves paper web rigidity for low basis weight paper
which results in better runnability on high speed printing presses
and folders used to produce magazines. Further, the thicker paper
produces a bulkier magazine which is less flimsy when handled. A
bulkier magazine "feels more substantial" i.e., it will not droop
or feel limp. Individual pages will separate easier and turn
without sticking together.
[0061] FIGS. 6A-6D schematically illustrate these different
lightweight coated papers of the prior art, and a lightweight
coated paper embodying the present invention, each of which has the
same total weight of 30 pounds/rm. The paper of FIG. 6A is
conventional lightweight coated paper and has a caliper of 1.6
mils., a base weight of 22 pounds and a coat weight of 4 pounds on
each side of the base. The paper of FIG. 6B is also a conventional
lightweight coated paper that was earlier made and sold by
Consolidated Papers, Inc. and that has a caliper of 1.8 mils, a
base weight of 23 pounds and a coat weight of 3.5 pounds on each
side of the base. The paper of FIG. 6C is likewise conventional
lightweight coated paper and has a caliper of 1.9 mils, a base
weight of 24 pounds and a coat weight of 3 pounds on each side of
the base. FIG. 6D shows a high bulk lightweight coated paper
according to the teachings of the invention, which has a caliper of
2.0 mils, a base weight of 25 pounds and a coat weight of 2.5
pounds on opposite sides of the base.
[0062] It should be understood that the coating can be applied by
any of the coaters discussed herein including a film coater or
speed coater. As used herein, the term "blade coater" includes such
film and/or speed coater.
[0063] The following table compares the effects of hot-soft
calendering versus supercalendering of high bulk coated paper of 32
pound weight, where FPM means feet per minute, PLI means pounds per
lineal inch, RH means relative humidity, MD means machine
direction, W means web side and F means felt side:
Effect of Hot/Soft Calender vs. Super
[0064]
10 Hot/Soft Sample Supercalender Calender Identification # B641122
B641109 Web Speed - FPM 2000 2500 Nip Load - PLI 1150 1500
Temperature - .degree.F. 200.degree. 275.degree. Number of
Nips/Side 4 2 Basis Wt. (73.degree./50% RH) 32.7 32.9 Coat Wt. W/F
3.1/3.2 3.1/3.2 Caliper - mils 1.89 2.00 Bulk Factor 57.7 60.7
Gloss 42/40 38/40 Opacity 89.3 90.1 L&W Stiffness - MD 59 69
Parker Printsurf W 1.92 2.23 F 2.34 2.30 Heidelberg Print Print
Gloss W 54 49 F 46 52 Print Density W 1.36 1.30 F 1.31 1.31 Print
solid W 4 5 F 4 5 50% Halftone W 7.7 7.1 F 6.0 7.2 Pickouts W 54 53
F 52 54
[0065] The following table shows parameters involved in the
production of 32 pound lightweight coated having a 75.degree. TAPPI
gloss of 45:
11 Reels Control Trial 95% Conf. Significance Std / Trl Average
Average Difference interval SUPERED TESTS Basis wt. ** 8 / 4 32.0
31.8 -0.2 .+-.0.2 Callper *** 8 / 4 18.3 18.2 1.9 .+-.0.5 Bulk ***
8 / 4 50.8 57.2 6.4 .+-.1.6 Opacity 8 / 4 88.1 88.0 -0.1 .+-.0.8
Gloss Wire * 8 / 4 45 43 -2 .+-.2.0 Gloss Felt * 8 / 4 45 44 -1
.+-.0.9 Print Surf Wire *** 8 / 4 1.5 1.7 0.2 .+-.0.1 Print Surf
Felt *** 8 / 4 1.6 1.8 0.2 .+-.0.1 L&W *** 8 / 4 42 47 5
.+-.2.2 HEIDELBERG / Ink Density Wire ** 2 / 4 1.44 1.36 -0.08
.+-.0.0 Ink Density Felt ** 2 / 4 1.40 1.36 -0.04 .+-.0.0 Ink Gloss
Wire *** 2 / 4 62 54 -8 .+-.2.7 Ink Gloss Felt *** 2 / 4 58 54 -4
.+-.1.6 I.A. 50% Halftone W * 2 / 4 6 7.8 1.8 .+-.1.6 I.A. 50%
Halftone F 2 / 4 6.2 7.3 1.1 .+-.2.4 I.A. 75% Halftone W 2 / 4 5.4
5.8 0.4 .+-.1.6 I.A. 75% Halftone F 2 / 4 5.5 8.4 0.9 .+-.3.4
***Significantly different @ 99% confidence level. **Significantly
different @ 95% confidence level. *Significantly different @ 90%
confidence level.
[0066] The following table shows various average results obtained
with 32 pound lightweight coated paper of and made according to the
present invention:
12 AVERAGE TEST RESULTS Sample # 970092 970098 970102 9790083
Identification Control Trial 1 Trial 2 Trial 3 Reel # B641122
B6411096 B8411059 B841109 Finte/ft/mg SPC @ Weight H/S @ S.P. H/S @
3 P H/S @ Belair Web Speed 2000 2500 2500 4000 POOLED Nip Load PLI
1150 1500 1500 1500 STD. Temperature, .degree. F. 200 275 325 250
DEV. Basis Weight (Cond.) 1 32.7 32.9 33.0 33.1 Coat Weight - W 1
3.1 3.1 3.1 3.1 Coat Weight - F 1 3.2 3.2 3.2 3.2 Ash 1 18.0 17.5
17.5 17.4 Callper 8 1.89 2.00 2.02 2.02 0.02 Bulk 8 57.7 60.7 61.2
61.0 0.8 75.degree. Paper Gloss - W* 8 42 38 36 38 1 75.degree.
Paper Gloss - F 8 40 40 38 36 1 Brightness - W 2 70.1 68.4 86.8
57.9 0.2 Brightness - F 2 71.5 68.4 67.6 68.1 0.8 Color `a` - W 2
-0.1 -0.1 -0.1 0.0 0.0 Color `a` - F 2 0.2 0.1 0.3 -0.1 0.1 Color
`b` - W 2 3.2 4.1 4.8 3.9 0.2 Color `b` - F 2 2.5 3.9 4.3 4.1 0.4
Opacity 8 89.3 90.1 90.4 90.0 0.4 Undertone - W 2 4 4 4 5 0
Undertone - F 2 4 4 4 5 0 Micro. Galv. - W 2 4 4 4 3 0 Micro. Galv.
- F 2 4 4 4 3 0 Tensile 8 11.1 10.5 10.8 10.6 0.7 Tear C.D. 4 25.3
25.4 24.6 26.6 0.5 L&W Stiffness 8 59 69 88 87 2 Scott Bond 5
176 177 179 185 8 H.P.D. 8 127 117 101 110 10 Print Surf - W 8 1.92
2.23 2.33 2.72 0.10 Print Surf - F 8 2.34 2.30 2.46 2.48 0.08 Croda
Holdout - W 2 60.0 58.5 60.0 59.0 1.1 Croda Holdout - F 2 61.5 60.0
62.0 61.0 1.1 Water Drop - W 2 10 12 12 10 1 Water Drop - F 2 10 11
12 9 1 IGT, #3 @ 3.5 m/s - W 4 88 111 75 116 11 IGT, #3 @ 3.5 m/s -
F 4 70 98 102 108 11 Prufbau Dry Pick - W 2 4.0 4.0 4.0 4.0 0.0
Prufbau Dry Pick - F 2 4.0 4.0 3.0 4.0 0.0 Prufbau Wet Pick - W 1
5.0 5.0 5.0 4.0 Prufbau Wet Pick - F 1 4.0 5.0 4.0 4.0 Adams Wet
Rub - W 2 1.1 0.9 1.0 1.0 0.2 Adams Wet Rub - F 2 1.6 1.0 1.2 1.1
0.1 Sutherland Rub - W 2 4.0 4.0 4.0 4.0 0.0 Sutherland Rub - F 2
4.0 4.0 3.5 4.0 0.0 VC Absorbency - W 4 89 91 96 90 4 VC Absorbency
- F 4 91 94 91 91 2 Heidelberg Halftone - W 1 8 5 6 4 Heidelberg
Halftone - F 1 4 5 5 4 Heidelberg Solid - W 1 4 5 8 4 Heidelberg
Solid - F 1 4 5 5 7 Heidelberg 50% Halftone - W 3 7.7 7.1 8.7 8.1
0.3 Heidelberg 50% Halftone - F 3 8.0 7.2 8.2 8.9 0.5 Heidelberg
75% Halftone - W 3 2.7 4.3 4.8 1.8 1.5 Heidelberg 75% Halftone - F
3 2.9 5.9 5.4 2.7 1.5 Heidelberg Ink Gloss - W 1 54 49 48 48
Heidelberg Ink Gloss - F 1 46 52 50 44 Heidelberg Ink Density - W 1
1.38 1.30 1.33 1.33 Heidelberg Ink Density - F 1 1.31 1.31 1.32
1.30 Heidelberg Coating Pick - W 1 25 33 38 34 Heidelberg Coating
Pick - F 1 28 38 42 35 Heidelberg Total Picks - W 1 54 53 54 53
Heidelberg Total Picks - F 1 52 54 51 50
[0067] The present invention is usable in conjunction with papers
for web offset, rotogravure, flexographic, letterpress and
others.
[0068] As used herein the term lightcoat weight refers to papers of
30-40 pounds per ream and ultra light coat weight refers to papers
of 24-28 pounds per ream. The present invention contemplates
producing lightweight coated paper of high bulk with a gloss of 40
or above, and in fact Consolidated Papers, Inc. has achieved a
gloss of 45. For ultra lightweight coated papers of high bulk, the
present invention contemplates a gloss of 35.
[0069] While embodiments of the invention have been described in
detail, various modifications and other embodiments thereof may be
devised by one skilled in the art without departing from the spirit
and scope of the invention, as defined in the appended claims.
* * * * *