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Patent 1054293 Summary

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(12) Patent: (11) CA 1054293
(21) Application Number: 1054293
(54) English Title: THERMOSETTING PHENOL-FORMALDEHYDE RESINS
(54) French Title: THERMODURCISSEMENT DE RESINES DE TYPE PHENOL-FORMALDEHYDE
Status: Term Expired - Post Grant Beyond Limit
Bibliographic Data
(51) International Patent Classification (IPC):
  • C08G 08/10 (2006.01)
  • B22C 01/22 (2006.01)
  • C08J 03/11 (2006.01)
  • C08L 61/10 (2006.01)
  • C08L 97/02 (2006.01)
  • C09J 16/06 (2006.01)
(72) Inventors :
  • CHANDRAMOULI, PITCHAIYA (Canada)
  • VASISHTH, RAMESH C. (Canada)
(73) Owners :
(71) Applicants :
(74) Agent:
(74) Associate agent:
(45) Issued: 1979-05-08
(22) Filed Date: 1975-04-16
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data: None

Abstracts

English Abstract


ABSTRACT OF THE DISCLOSURE
Thermosetting pheno-formaldehyde resins having novel
structures and properties are described. The resins are formed
at a mole ratio of formaldehyde to phenol of above 1.7:1 in an
aqueous reaction medium. The resins form acid-catalyzed, room-
temperature stable and mobile resins which may be applied as is
onto substrates for the formation of molded articles, such as rice
husk boards.


Claims

Note: Claims are shown in the official language in which they were submitted.


The embodiments of the invention in which an exclusive
property or privilege is claimed are defined as follows:
1. A room temperature-stable, acid-catalyzed and mobile
thermosetting phenol-formaldehyde resin capable of rapid cure at
elevated temperature, formed by reaction of formaldehyde and
phenol in an aqueous reaction medium in the presence of a metal
carboxylate therefor at a mole ratio of formaldehyde to phenol
of greater than about 1.7:1 and acid catalysis of the resin so
formed, and having a viscosity of about 1000 to 40,000 cps at
75°F.
2. The resin of Claim 1 wherein said mole ratio is from
about 1.8:1 to about 3.0:1.
3. A method for the production of a room temperature-
stable, mobile thermosetting phenol-formaldehyde resin capable
of rapid cure at elevated temperature which comprises:
reacting phenol and formaldehyde together in a mole
ratio of formaldehyde to phenol greater than about 1.7 to 1 in
an aqueous medium in the presence of a water-soluble metal
carboxylate catalyst therefor to form a thermosetting phenol-
formaldehyde resin having benzyl ether linkages ortho to the
phenolic hydroxyl group and an infra-red spectrum which dis-
plays large absorption at wave numbers of 1230 cm-1 , 1060 cm-1
and 1030 cm-1,
reacting said resin with at least one strong acid to
cause a decrease of at least 5% in said absorption at wave
number of 1060 cm-1 and an increase of at least 5% in said
absorption at wave number of 1030 cm-1 while leaving substantial-
ly unaffected said absorption at wave number of 1230 cm-1, and
isolating the phenol-formaldehyde resin so formed.
4. The method of Claim 3 wherein said phenol and
18

formaldehyde are reacted together in a single step carried out
wholly at a temperature above about 90°C.
5. The method of Claim 3 wherein said strong acid is
para-toluene sulfonic acid.
6. A composition comprising a free flowing mass of sub-
divided material consisting of individual elements having a
coating over at least part of the surface thereof of a room
temperature-stable, acid-catalyzed and mobile thermosetting phenol-
formaldehyde resin capable of rapid cure at elevated temperature,
formed by reaction of formaldehyde and phenol in an aqueous
reaction medium in the presence of a metal carboxylate catalyst
therefor at a mole ratio of formaldehyde to phenol of greater
than about 1.7:1 and acid catalysis of the same, and having a
Viscosity of about 1000 to 40,000 cps at 75°F.
7. The composition of Claim 6 wherein said individual
elements are grains of foundry sand.
8. The composition of Claim 6 wherein said individual
elements are rice husks.
9. The composition of Claim 6 wherein said individual
elements are wood chips.
10. The composition of Claim 6 wherein said individual
elements are wheat straw.
11. The composition of Claim 6 wherein said individual
elements are rye grass.
19

Description

Note: Descriptions are shown in the official language in which they were submitted.


1~)54'~93
This inv~ntion relates to novel thermosetting phenol-
formaldehyde resins and to their preparation.
In our Canadian Patent No. 1,015,889 there is described
the production of certain novel thermosetting phenol-formaldehyde
resins having a characteristic infra-red spectrum and containing
benzyl ether linkages ortho to the phenolic hydroxyl group.
It has now been found that resins formed from mole
ratios of formaldehyde to phenol of above about 1.7:1 have unique
properties and characteristic infra-red spectra not exhibited by
resins formed from mole ratios of formaldehyde to phenol of less
than about 1.7:1.
Thus, while the resins all have high absorbance at a
wave number of 1230 cm 1, the resins formed from a greater than
1.7:1 mole ratio exhibit a strong absorption at a wave number of
1030 cm l, a peak which is absent from the spectra of resins
formed from less than 1.7:l mole ratios.
. Further, the ratio of absorbance at a wave number of
1030 cm 1, measured from a base line drawn between wave numbers
of a wave number of 1130 cm 1 and a wave number of 9S0 cm l, to
that at a wave number of 1230 cm , measured from a base line
between wave numbers of 1130 cm 1, and 1310 cm l is greater than
0.67 in the spectra of the no.vel resins.
The novel resins of this invention exhibit properties
- which lead to novel, unexpected and advantageous uses for resins
formed from mole ratios of formaldehyde to phenol greater than
about 1.7:1.
These novel properties arise from the differences in
structure of the resins produced at the different mole ratios.
Thus, for a given solids loading, catalyst level based on phenol
and reflux time, the resin viscosity decreases as the formaldehyde
to phenol mole ratio increases and the resins cure rapidly at

1~54293
high temperatures of about 200C. However, the stability of
the resins, after addition of acid catalyst, at room or near
ambient temperatures of about 20 to 25C increases with in-
creasing formaldehyde
- 2a -
, . ,~.. ,

to phenol mole ratios. ~S4
In typical end uses of resole-type phenol ~ formaldehyde
resins, it is common practice to accelerate the rate of cure or
thermosetting of the resins by the addition of small quantities
of acid catalysts, such as, benzene sulfonic acid and para-
toluene sulfonic acid.
Non-caustic resole-type phenol-formaldehyde resins
that have an infra-red spectrum exhibiting high absorption at
wave numbers of 1010, 1060 and 1230 cm are used for certain
1~ applications, such as rice husk board manufacture, and have a
high viscosity at room temperature. These resins require heating
to lower their viscosity before application to a substrate. Since
such resins cure rapidly in the presence of acid at the elevated
temperatures required for application to the substrate, resin and
acid have to be applied separately to the substrate. (For example,
see our U.S. Patent No. 3,850,677).
This mode of application is haphazard at best since
proper contact of acid and resin on the substrate surface is by
no means assured, and this has lead to ~he use of greater quan-
tities of acid than otherwise would be required, resulting inuneconomic chemical use and often impaired product appearance.
However, at mole ratios of formaldehyde to phenol above
1.7:1, the viscosity of the resin is such as to allow near room tem-
perature application and, after acid addition, for example, up-to
about 2 to 3% of para-toluene sulfonLc acid, the resin exhibits
stability which allows long storage before use and the application
of the resin to the substrate in an acid cataly~ed form, thereby
avoiding the necessity to apply catalyst separately.

105~293
Since a single-component, acid-catalyzed, room
temperature-stable and rapidly-curable resin may be provided in
accordance with this embodiment of the invention for application
t~ the substrate in end uses of the resin, the quantity of acid
catalyst required for adequate curing of the resin is considerably
decreased, typically to about l/6th to l/lOth of that required
when the resin and catalyst are applied separately, as required
in the prior art, thereby leading to more economic utilization of
materials and a vastly improved product appearance, especially in
rice husk board production.
- Additionally, resins prepared using mole ratios of
formaldehyde to phenol of greater than 1.7:1 require a viscosity
of about 1000cps or more at 75 F to perform as satisfactory
adhesives for rice husk boards.
One embodiment of the present invention, therefore,
provides a room temperature-stable, acid-catalyzed and mobile
thermosetting phenol-formaldehyde resin capable of rapid cure at
elevated temperature, formed by reaction of formaldehyde and
phenol in an aqueous reaction medium at a mole ratio of formal-
dehyde to phenol of greater than about 1.7:1 and having a viscosityof from about 1000 to about 40,000 cps at about 75F.
The resins formed from a mole ratio of formaldehyde to
phenol greater than about 1.7:1 may be used in a variety of useful
adhesive applications. For example, the resins may be used in
various spray applications, such as rice husk board and particle
board production. The resins also may be used in paper lamination,
foundry core applications and plywood production.
In cold set foundry applications for making core mould~,
phenolic resins are commonly used. The resins used, however, are
not the conventional resole-type resins but are generally modified
with expensive and scarcely-available chemicals, such as furfuryl

~054Z93
alcohol and silanes. It was surprising to find that the resins
of the present invention, while being very stable in the presence
of small quantities of acid-catalysts, at room temperature, react
rather rapidly at acid levels of about 20 percent or more and are
quite suitable for cold set, room temperature cure type appli-
cations.
A further surprising property is-the ability of these
resins to cure under the influence of radio frequency. Radio
frequency, for example, is commonly used where faster production
cycles are required. Typical examples are scarf and end joining
and preheating of mats in panel board manufacture. The con-
ventional caustic-containing phenolic resins, however, are not
suitable for these applications as they arc very heavily under
the influence of the high frequency energy and tend to precure.
More sophisticated resins, such as the resorcinol-modified resins
catalyzed with para formaldehyde are suitable for use under radio
frequency. Such resins are not only prohibitively expensive but
have very poor pot life.
However, when the resins of this invention, produced
-20 from mole ratios of formaldehyde to phenol of at least 1.7:1 are
used in plywood manufacture with radio frequency preheating, con-
siderable benefits in production cycles are derived.
The resins of this invention preferably are formed by
a one-step process in which phenol and formaldehyde are reacted,
in quantities such that the mole ratio of formaldehyde to phenol
exceeds about 1O7:1, in an aqueous reaction medium containing a
metal carboxylate catalyst for the reaction, for example, zinc
acetate, wholly at a temperature above about 90C, as described
in more detail in copending Canadian Application Serial No.
225,026 filed concurrently herewith.
The resin formed by this procedure exhibits large
5 -
.._ -

1054'~g3
absorption at wave numbers of '230 cm 1, 1060 cm 1 and 1030 cm 1.
Upon addition of at least one strong acid to this resin, there
results a decrease of at least 5% in the absorption at a wave
- 5a -
, ~".

054~3
number of 1060 cm and an increase of at least 5% in the
absorption at a wave number of 1030 cm while leaving substan-
tially unaffected the absorption at a wave number of 1230 cm 1
The latter thermosetting phenol-formaldehyde resin may be
isolated.
The invention is illustrated by the following Examples.
In these Examples reference is made to the accompanying drawings,
in which Figures 1 to 12 are infra-red spectra of a number of
thermosetting phenol-formaldehyde resins.
Example 1
This example illustrates the formation of a phenol~
formaldehyde resin of the present invention.
Into a glass reaction vessel equipped with an agitator,
a reflux condenser and a thermometer was charged 179~.1 g tl9.09
moles) of phenol, 2788.3 g (34.35 moles) of formaldehyde having a
methanol content of less than 1.5 wt.% (corresponding to a
formaldehyde to phenol mole ratio of 1.8:1), 144.8 g (0.034 moles
and about 8 wt. ~ is based on phenol) of ~inc acetate dihydrate
and 772.8 g of water, to provide a reaction mixture having a
total reactants loading of 54.01%.
The mixture was heated rapidly to go + 2 C in 40+ 5
minutes. The temperature was raised further to reflux,
tapproximately 100 C) over the next 15 minutes by controlling the
rate of heating. The reaction mixture was kept under constant
reflux for a total time of 210 minutes. About 105 minutes after
commencement of the reflux began, a distinct phase separation was
observed.
After the completion of the reflux period, the reaction
mixture was cooled to 35 C and the agitation stopped. Cooling
then was continued to about 25 C. The liquid resin phase was
separated from aqueous phase. The resin was found to have a
Brookfield viscosity of 2000 to 2300 cps at 120 F and a N.V.
solids content of 75 to 80 percent.
-- 6

10542g3
Example 2
-
This example illustrates the different structures
obtained when resins are formed from different mole ratios o~
formaldehy~e to phenol.
A series of phenol-formaldehyde resins was prepared
following the procedure of Example 1 using ~arying mole ratios
of formaldehyde to phenol. An infra-red spectrum was taken
for each resin.
To a sample of each resin was added 1% para ~oluene
1~ sulfonic acid (used as a 50% aqueous solution) and the infra-red
spectrum again taken. The two sets of spectra appear as
Figures 1 to 12, identified as follows:
Figure 1 Mole ratio 1.4:1 No acid
Figure 2 Mole ratio 1.6:1 No acid
Figure 3 Mole ratio 1.8:1 No acid
~igure 4 Mole ratio 2~0:1 No acid '
- Figure S Mole ratio 2.5:1 No acid
Figure 6 Mole ratio 3.0:1 No acid
~igure 7 Mole ratio 1.4:1 Acid Added
- 20 Figure 8 Mole ratio 1.6:1 Acid Added
; - Figure 9 Mole ratio 1.8:1 Acid Added
Figure 10 Mole ratio 2.0:1 Acid Added
Figure 11 Mole ratio 2.5:1 Acid Added
Figure 12 Mole ratio 3.0:1 Acid Added
- It will be seen from a comparison of the spectra
of the resins both before and after acid addition that there is
a clear strong absorption peak at a wave n~ber of 1030 cm 1 in
the spectra of the 1.8 and above mole ratio resins whereas this
peak is absent from the spectra of the 1.4 and 1.6 mole ratio
resins.
-- 7

1054Zg3
Fur~her, a comparison can be made between the ratios
of absorption at a wave number of 1030 cm 1, measured from a
base line drawn between ~ave numbers 1130 cm and 950 cm 1, to
that at a wave number of 1230 cm 1, measured from a base line
between wave numbers of 1130 cm and 1310 cm
Analysis of the spectra of the 1.8:1 and above mole
ratio materials reveals that prior to acid addition there is
also a large absorption at a wave number o~ 1060 cm 1, and after-
acid addition, there is a decrease in the absorption at a w~ve
number of 1060 cm 1 and an increase in adsorption at a wave number
of 1030 cm 1, In the case of the 1.6:1 and below mole ratio
resins, the adsorption at a wave number of 1060 cm 1 increases.
.
The following Table I provides the appropriate
comparisons:
- ~ . . ' - : -
: . . .
.. -
",.' ~ ., . , ~
' ,' , . , ' ' - . ' .
,'' ~' ~. ' , .
. ~ ' '
'-
. ' ' ' ' ' .
. ' ' .

10542~3
G~
,_ ~ ~ ~ ~9
.
U~ ~ ~1 ~ O
,, ~ ,,
~) +, + + + +
d~
-I
,, .~
t, ~. o
~¢-~ ~ CO ~ ~ e~
o o ~ ~ ~ ,
~ ~ S~-~ ~ ~ OD
o ~ ~ ~;
, ~ o o o o
W ~
o ~ ..
.
. ...
,
t) ~ ' a~
~,o ~ ~ ,~
co a~ O ~ ~~
~.~ ~ U~I~ ~ ~ . o U~ -
o~
- m~ ~ 5
~,
a), ~1 . '
C5~ 1~O ~1 0 1
. ~ U7t~ o
~C ~ + ~~1
C~ + II I I O
. . ~
C . .
- _I - c~ o c~ r o
H O S~-rl ~ . .
~!l~ C~OOOO0:U~
O O
~:1 u~ ~ ~1 ¢ u~
. ~ O F~ .
O ~J
¢ o
1 ~ ~r - o er a~ ~ o
- ~-~U~~ ~`- CO ~ o
- o ~o . . .. . . U~
'. o ~ o o oo o ,~
m
'. ~
': - O E~
~r~ .
~,
_
tt;
~ _I~1 ~~ ~1 -
a~ .. .. .. .. .. .. Q~
0 0 ~n o ~
0 ,~ N ~ Z

~059~Z93
I~ will be seen from the above Table I that the resins
of mole ratio 1.8:1 and above not only have a distinct peak at
a wave number of 1030 cm 1 but also a ratio of absorbance ~o
that at a wave number of 1230 cm 1 greater than about 0.6, both
before and after acid addition, whereas resins of mole ratio
1.6:1 and below not only do not exhibit such a peak at a wave
number of 1030 cm 1 but also have a ratio of absorbance to that
at a wave number of 1230 cm 1 less than 0.6, both before and
after acid addition.
Example 3
This example illustrates the physical properties of
phenol-formaldehyde resins formed at various mole ratios of
phenol to formaldehyde.
A series of phenol-formaldehyde resins were prepared
following the procedure of Example 1. Various properties of the
resins were tested and the results are reproduced in the
- following Table II:
'' ' .' ' .
.
,

-
l ~ ~
o. ~ lOS4Z~3
~1
ol ~ a~ .~ .~ .~ .
, ~ ~ W ~ ~ ~
o ,~ .,,
o o ~ U7 U~ 0 ~q
~4
~ -3 ~
Cv __ I
~ ~q
.~ ~ ~ o ,. ~ ~ ~ ~
E~ ~ ~ 1
~o,
. oO
. . _ ~ ~ ~
~n ~ o o o
rl N O O O o O O O ~ 1
~ ~ O O O o o O O 11~ 0 X
.~ ~ ` ` ` o o o ~ 3 q~ o
a) ~ o o o ~ a~
Q~ ~ o U~ '~ o CO ~ -I
O i~ r' ~ ~u~ o 'I " ~
~ C~ . ~1 ~ v
p~ U~ . ~V
~ . , _ ~
. . .~
U1~ O O O O ~ v
~ ~ ~O O O o O O ~ .~
~ ~ ` ` O O O O .
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~1 e o o O O O O O O o o s, ~:
. ~ ~ O O ~ ", ,~ ,~, CO .,, U~
. O ~ ~ , .
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' _ U~
.' . . ~ . 0~O ,~ o
: ~ . . o a) ~
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- H . . ~ I I I . 0 v~
- H l ~ ~ 1 ~ ~ X X ~ 15 3
1~3 . .
O . . . 0~1 ~ ~ 11
E ~ ~E4 . . . u~O O
. .~ O ' CO ~ ~ 'O O o U~ ,S t71 ~
~n ~ .~ r ~ ~ . ~ ~ S -
i O . ~1 ~ co ~ u~ . U~.~ h ~O ~ s::
- , .~ ~o ~ ~ ~ . ~ v ~'3-~
~ ~ ., ~ ." .
. _I v~ 0 ~~ $ ~ ~ o
. ~ U U U . S ~ ~ v~
. - . .- G~O~ 0 0 ~ ~ Cv
! 4~ ~ ~ ~ o o o o ~ 3 ~ ~ 0 u~
: X ~1 - S ~ o ~ er ~ ~5 0 o ~
. . O u~ ~ 1 N 1: U~ O U~ 0
h ~ ::C mm ~ ,~ ~ r~s 3 ~,,
! 1~ . 0 ~-1 ~3 .,_1 ,_1 ~
. _ _ ~ h 0~.1t;l s::
: ~ ~ O
., ~P . ~ g ~ ~ O ~ O '
!~ . 0 d (U ~ ~v ~~l
,O ~ ~ n ~ C C D~
O~ C) ~ O t~
~ ~ ~ v0
. . . ._
O '
P~ ~ ~ ~
~ ..
~v ~ ~ In ~3 ou~ o o 0
.~ Q~ . . . . . . . . ~v
d ~ ~ 1
~ ~ . . X
11
.

1054~93
The results of the above Table II indicate the
decreasing viscosity of the resins at mole ratios of 1.8:1 and
a~ove, the decreasing electrical resistance of the resins at
mole ratios of 1.8:1 and above, the rapidly-decreasing cure times
of acid catalyzed curings with increasing mole ratio and the
ability to emulsify the resins at mole ratios of 1.5:1 and
above.
The results of the above Table II also show that,
contrary to the expectation of one practising this art, the
electrical properties of the resins and the change in electrical
properties of the resins after acid addition are independent of-
the viscosity of the resin.
.~' ' '',. "~' , ~ .
.
. ' : ' ~ . .. .
,
:' : "' - ' '' .. '
- , :
' ,~ , ' ,
'
~- , -
. 12

1054X~3
ample 4
This example illustrates the ~ormation of rice husk
- board from acid catalyzed resins.
A 75% solids resin formed by the procedure of Example
1 and having a mole ratio of formaldehyde to phenol o 1.6:1 was
catalyzed with 0.5~ by weight of para-toluene sulfonic acid (used
as a 50% solution) and was found to be stable at room temperature
for o~er 24 hours. The resin, however, was incapable of being
sprayed at room temperature due to its inherent viscosity
~50,000 cps at room temperature) and consequently had to be
warmed to 160F for use. At this temperature, the resin gained
- viscosity rapidly and hence could not be spray applied to the
rice husks.
- The resin and acid catalyst, however, were capable of
being satisfactorily applied to the rice husks as separate com-
ponents. The acid first was sprayed onto samples of cleaned
rice husks at levels of 4~ and 8% based on resin weight. There-
after, ~he resin was hot meit sprayed at 150F onto the rice
husk samples, in both cases at a resin solids leve~ of 10~ based
~0 - on husks. The resin coated husks were laid into mats, consolida-
ted and then pressed in a hot press at 390F for a period of 11
- minutes.
An equivalent 75% solids resin formed by the procedure-
of Example 1 and having a mole ratio of formaldehyde to phenol of
1.8:1, after catalyzing with 0.5% by weight of para-toluene sul-
fonic acid (used as a 50% aqueous solution), was found to be
stable at room temperature for prolonged periods of over a week.
The catalyzed resin was found to be sprayable at room tempera~ure
and near ambient temperatures of 80 to 90F and rice husk boards
were formed by spraying the cleaned husks with 10% of the acid
catalyzed resin, followed by the mat formation, consolidation and
hot pressing as outlined above. The resultant board of 1/2 inch
_ 13

~054293
thickness and 48 lb/ft3 density was very light in colour,
in contrast to the typical rice husk boards formed from
the two-component system which were quite dark in colour.
Similar rice husk boards were formed from one-
component systems using resins at other mole ratios above
1.7:1.
The strength properties of the boards were
determined and the results appear in the following Table
III:
TABLE III
.
Type of Application Mole Ratio Catalyst Intemal Mbdulus of
Level ~ Bond Rupture
Strength psi
psi
Two-component 1.6:1 4 Dela~inated
Two-component 1.6:1 8 75 1900
One-component 1.8:1 1 90 2100
One-component 2.0:1 108
One-component 2.5:1 76
One-component 3.0:1 55
One-component 3.0:1* 57
*-Deferred feed
The results of the above Table III clearly
-
demonstrate that the abillty of a 1.8:1 mole ratio resin
to be l~sed in a one-component spray application leads to
the production of good quality rice husk boards with
improved appearance and considerably lower catalyst levels
than are required when a 1.6:1 mole ratio resin is applied
in a two-component spraying procedure, the latter
procedure being adopted due to the inability of the 1.6:1
mole ratio to be sprayed as a single component in a
commercially-feasible manner.
~ - 14 -

1054Z93
The results of the above Table III also demon-
strate that good quality rice husk boards can be formed
even from the very low viscosity resins provided at mole
ratio of 3.0:1.
It has already been demonstrated in our U~S.
Patent No. 3,850,677 that resins of 1.6:1 mole ratio of
low viscosity at room temperature are not suitable for
the manufacture of rice
- 14a -

- lOS4293
~nusk boards. The l~ter low viscosity resirs typically are
prepared by the procedure-outlined in Canadian Patent No. 927,041
- at mole ratios of about 1.5:1.
Example 5
This example illustrates the use of various phenol-
: formaldehyde resins in cold set foundry sand applications.
Sand was coated with 1.5~ by weight of resin andvarying amounts of catalyst levels by tumbling the mix in a
tumbler. Cylindrical molding forms were made in a mold and
allowed to ary under ambient temperature conditions. The forms
were tested at various intervals for strength properties.
: .
: ~ The results are reproduced in the following Table
IV; along with comparative data on commercially-available
~-~ - resins: .
-
: . ' : ,,
',' . ' - , - ' '
.. . .. . ~
: ~ .
~ . .
.
.
: -- .
.: - - . ,

o~ 1054'~93
O It) O ~: L'~ O
~1' 'I ~ 1` 0
1~1 O ~ o~P . . Il~ O ~ ~
1~) r-l 11~ O ~ 'I ~) ~ O ~1 1¢
-
'a ~: h
O a~
'r o R d~
o U~ U~ U~ o U~ ~ o
o ~1 ~ ~ a~
o ~ ~ ~ G~ O ~J
_I o o ~ ~J ~ ~ a~ X
dP
U~
_,
. - .
~# In o u~
o ~ ~I c~
~r o ~D
U') _I ~ tx~ t O Sl ~C
~ . a~ .
U~
O U~
U~N ~ ~ O
O _I. dP ~ N
o ~ . .er co noo '9 o a~
_I 1~~--I~1 N N ~ 0
~ - -. . .. ~
. ., E~,
O ~OP~ O ' ` ..
._ O ` dP O u~) O
H O CO~O 11') C'`l ~ O O O L'~
_I N C~ . . r`
1~ . , . O r-~ L~
E- ,~ ,

U~
E~
O Ll~O p~ . ~ O O O O O
O _I ~ N N L) lr)
~ . . . . . u~
,.1 1~) O N d' ~r t~ ~ I~
~ ~o ~1 -I ~ ' .
O .
~¢ . 3
O 1~N E~ ~r O
1~O
o ~r . . . . u~
~1 ~P o ~ ~ In~D ~ ~ `'
U~
_, . . ' O
.
Et
O U~O ~ ~ ~0 0 0 0 0 0
O ,~ . ~ u~ o o U~
O ~ cP . . . . u~
Lt~ O ~i ~D ~ O a~ I~ rl
0~ ~1 ~ ~ ~
. ~ In
U _ 0 :~
~ 0 ,~ H
O
~ _ _
O s ~ 4
0 ~ U)~ ~ 0 -
td ,,~ Z ~'
16

1054Z93
The results of the above Table IV indicate the sui~-
ability of the resins of mole ratio of 1.8:1 in cold foundry sand
- applic~tion. These results are in contrast to experiments con-
~ucted with resins formed at a mole ratio of 1.6:1 which showed
that similar mouldin~ ~orms could not be made at the catalyst
levels of 20~ or more outlined in Table IV. Considerable precure~
occurred and the resulting moulding forms lacked strength and
integrity.
It will be seen therefore that the present invention
provides novel resins which have superior adhesive properties in
many applications. Modifications are possible within the scope
of the invention.
- 17 -
;

Representative Drawing

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Administrative Status

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Event History

Description Date
Inactive: IPC from MCD 2006-03-11
Inactive: IPC from MCD 2006-03-11
Inactive: IPC from MCD 2006-03-11
Inactive: Expired (old Act Patent) latest possible expiry date 1996-05-08
Grant by Issuance 1979-05-08

Abandonment History

There is no abandonment history.

Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
None
Past Owners on Record
PITCHAIYA CHANDRAMOULI
RAMESH C. VASISHTH
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

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Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Claims 1994-04-20 2 67
Drawings 1994-04-20 6 75
Abstract 1994-04-20 1 18
Descriptions 1994-04-20 19 500