JPH0441912B2 - - Google Patents
Info
- Publication number
- JPH0441912B2 JPH0441912B2 JP62036686A JP3668687A JPH0441912B2 JP H0441912 B2 JPH0441912 B2 JP H0441912B2 JP 62036686 A JP62036686 A JP 62036686A JP 3668687 A JP3668687 A JP 3668687A JP H0441912 B2 JPH0441912 B2 JP H0441912B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- pressure
- recording paper
- sensitive recording
- mipb
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002904 solvent Substances 0.000 claims description 44
- KWSHGRJUSUJPQD-UHFFFAOYSA-N 1-phenyl-4-propan-2-ylbenzene Chemical group C1=CC(C(C)C)=CC=C1C1=CC=CC=C1 KWSHGRJUSUJPQD-UHFFFAOYSA-N 0.000 claims description 11
- HKTCLPBBJDIBGF-UHFFFAOYSA-N 1-phenyl-2-propan-2-ylbenzene Chemical group CC(C)C1=CC=CC=C1C1=CC=CC=C1 HKTCLPBBJDIBGF-UHFFFAOYSA-N 0.000 claims description 9
- AMBHHSBRXZAGDZ-UHFFFAOYSA-N 1-phenyl-2,3-di(propan-2-yl)benzene Chemical group CC(C)C1=CC=CC(C=2C=CC=CC=2)=C1C(C)C AMBHHSBRXZAGDZ-UHFFFAOYSA-N 0.000 claims description 7
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N diphenyl Chemical group C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 40
- 239000000975 dye Substances 0.000 description 35
- 239000000203 mixture Substances 0.000 description 33
- 239000003054 catalyst Substances 0.000 description 32
- 238000006243 chemical reaction Methods 0.000 description 32
- 101000648997 Homo sapiens Tripartite motif-containing protein 44 Proteins 0.000 description 21
- 102100028017 Tripartite motif-containing protein 44 Human genes 0.000 description 21
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 20
- 239000004305 biphenyl Substances 0.000 description 20
- 235000010290 biphenyl Nutrition 0.000 description 20
- 238000011161 development Methods 0.000 description 18
- 238000000034 method Methods 0.000 description 17
- 239000000243 solution Substances 0.000 description 15
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 13
- 239000007795 chemical reaction product Substances 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 9
- 239000007864 aqueous solution Substances 0.000 description 9
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 9
- 239000013078 crystal Substances 0.000 description 9
- 239000003094 microcapsule Substances 0.000 description 9
- 238000003756 stirring Methods 0.000 description 9
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 230000009965 odorless effect Effects 0.000 description 7
- LIWRTHVZRZXVFX-UHFFFAOYSA-N 1-phenyl-3-propan-2-ylbenzene Chemical group CC(C)C1=CC=CC(C=2C=CC=CC=2)=C1 LIWRTHVZRZXVFX-UHFFFAOYSA-N 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 6
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- IAUKWGFWINVWKS-UHFFFAOYSA-N 1,2-di(propan-2-yl)naphthalene Chemical compound C1=CC=CC2=C(C(C)C)C(C(C)C)=CC=C21 IAUKWGFWINVWKS-UHFFFAOYSA-N 0.000 description 5
- 239000011521 glass Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000012046 mixed solvent Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 230000006207 propylation Effects 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- YJTKZCDBKVTVBY-UHFFFAOYSA-N 1,3-Diphenylbenzene Chemical group C1=CC=CC=C1C1=CC=CC(C=2C=CC=CC=2)=C1 YJTKZCDBKVTVBY-UHFFFAOYSA-N 0.000 description 4
- 229920000877 Melamine resin Polymers 0.000 description 4
- -1 alkyl biphenyl Chemical compound 0.000 description 4
- 125000000217 alkyl group Chemical group 0.000 description 4
- 239000003086 colorant Substances 0.000 description 4
- 230000000977 initiatory effect Effects 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- YZGXNRPNBJZAED-UHFFFAOYSA-N 1,2-di(propan-2-yl)naphthalene naphthalene Chemical compound C1=CC=CC2=CC=CC=C12.C(C)(C)C1=C(C2=CC=CC=C2C=C1)C(C)C YZGXNRPNBJZAED-UHFFFAOYSA-N 0.000 description 3
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 3
- 229920001807 Urea-formaldehyde Polymers 0.000 description 3
- 238000005804 alkylation reaction Methods 0.000 description 3
- 239000002775 capsule Substances 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 239000004927 clay Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 238000005538 encapsulation Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 3
- 239000011259 mixed solution Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000011541 reaction mixture Substances 0.000 description 3
- 239000000377 silicon dioxide Substances 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000029936 alkylation Effects 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 239000001045 blue dye Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000002091 cationic group Chemical group 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- SYSQUGFVNFXIIT-UHFFFAOYSA-N n-[4-(1,3-benzoxazol-2-yl)phenyl]-4-nitrobenzenesulfonamide Chemical class C1=CC([N+](=O)[O-])=CC=C1S(=O)(=O)NC1=CC=C(C=2OC3=CC=CC=C3N=2)C=C1 SYSQUGFVNFXIIT-UHFFFAOYSA-N 0.000 description 2
- 229920001568 phenolic resin Polymers 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000010555 transalkylation reaction Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- RMSGQZDGSZOJMU-UHFFFAOYSA-N 1-butyl-2-phenylbenzene Chemical group CCCCC1=CC=CC=C1C1=CC=CC=C1 RMSGQZDGSZOJMU-UHFFFAOYSA-N 0.000 description 1
- YYKBFGMYHQMXIL-UHFFFAOYSA-N 1-phenyl-2,3,4-tri(propan-2-yl)benzene Chemical group CC(C)C1=C(C(C)C)C(C(C)C)=CC=C1C1=CC=CC=C1 YYKBFGMYHQMXIL-UHFFFAOYSA-N 0.000 description 1
- 102100029103 3-ketoacyl-CoA thiolase Human genes 0.000 description 1
- 238000003547 Friedel-Crafts alkylation reaction Methods 0.000 description 1
- 101000841262 Homo sapiens 3-ketoacyl-CoA thiolase Proteins 0.000 description 1
- 238000012695 Interfacial polymerization Methods 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- CZZYITDELCSZES-UHFFFAOYSA-N diphenylmethane Chemical class C=1C=CC=CC=1CC1=CC=CC=C1 CZZYITDELCSZES-UHFFFAOYSA-N 0.000 description 1
- KWKXNDCHNDYVRT-UHFFFAOYSA-N dodecylbenzene Chemical compound CCCCCCCCCCCCC1=CC=CC=C1 KWKXNDCHNDYVRT-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- IVJISJACKSSFGE-UHFFFAOYSA-N formaldehyde;1,3,5-triazine-2,4,6-triamine Chemical compound O=C.NC1=NC(N)=NC(N)=N1 IVJISJACKSSFGE-UHFFFAOYSA-N 0.000 description 1
- SLGWESQGEUXWJQ-UHFFFAOYSA-N formaldehyde;phenol Chemical compound O=C.OC1=CC=CC=C1 SLGWESQGEUXWJQ-UHFFFAOYSA-N 0.000 description 1
- 238000004508 fractional distillation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910017464 nitrogen compound Inorganic materials 0.000 description 1
- 150000002830 nitrogen compounds Chemical class 0.000 description 1
- 229920003986 novolac Polymers 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- ODGAOXROABLFNM-UHFFFAOYSA-N polynoxylin Chemical compound O=C.NC(N)=O ODGAOXROABLFNM-UHFFFAOYSA-N 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 125000001424 substituent group Chemical group 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 description 1
- 150000004897 thiazines Chemical class 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 150000004961 triphenylmethanes Chemical class 0.000 description 1
- 125000001834 xanthenyl group Chemical class C1=CC=CC=2OC3=CC=CC=C3C(C12)* 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
- C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
- C09B67/0071—Process features in the making of dyestuff preparations; Dehydrating agents; Dispersing agents; Dustfree compositions
- C09B67/0083—Solutions of dyes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B41—PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
- B41M—PRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
- B41M5/00—Duplicating or marking methods; Sheet materials for use therein
- B41M5/124—Duplicating or marking methods; Sheet materials for use therein using pressure to make a masked colour visible, e.g. to make a coloured support visible, to create an opaque or transparent pattern, or to form colour by uniting colour-forming components
- B41M5/165—Duplicating or marking methods; Sheet materials for use therein using pressure to make a masked colour visible, e.g. to make a coloured support visible, to create an opaque or transparent pattern, or to form colour by uniting colour-forming components characterised by the use of microcapsules; Special solvents for incorporating the ingredients
- B41M5/1655—Solvents
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Color Printing (AREA)
Description
産業上の利用分野
本発明は感圧記録紙用染料溶剤に関し更に詳細
にはp−イソプロピルビフエニル、ジイソプロピ
ルビフエニル及びm−イソプロピルビフエニルの
特定割合の混合物又はp−イソプロピルビフエニ
ルとジイソプロピルビフエニルの特定割合の混合
物からなる感圧記録紙用染料溶剤に関する。
先行技術
感圧記録紙は、電子供与性の呈色反応性を有す
る発色剤を有機溶剤に溶解しマイクロカプセル中
に内包させて支持体上に塗布した発色体シートと
発色剤と接触すると発色する顕色剤を他の支持体
上に塗布した顕色剤シートから成つている。
近年、感圧記録紙は、カーボン複写紙又は顔料
タイプの裏カーボン複写紙にかわつて広く使用さ
れている。このような、感圧記録紙としては、優
れた発色性、長期間保存の安定性及び耐光性を有
し、更に毒性が少なく且つ公害問題の起らないも
のであることが必要である。
感圧記録紙における発色剤(染料)を溶解させ
る溶剤としては次の要件を具備していることが要
求される。
(1) 発色剤の溶解度が高いこと。
(2) 発色剤の分解・発色などの変化を与えないこ
と。
(3) かなり沸点が高く、熱乾燥工程や高気温の所
でも蒸散しないこと。
(4) カプセル化の際水に溶出しないこと。
(5) 発色速度及び発色濃度が高く且つ発色後の色
調安定性が高いこと。
(6) 光、熱及び化学薬品に対して安定であるこ
と。
(7) カプセルが破壊された時カプセル内からの流
出が自由に行なわれるように低粘度であるこ
と。
(8) 臭いが実質的にないこと。
(9) 人体に対して毒性が低く、且つ安全であるこ
と。
(10) 生分解性が良く環境汚染を起さないこと。
このような要求を満す感圧記録紙用染料溶剤と
して、次のような溶剤が提案されている。
発色剤の溶剤として炭素数1〜12のアルキル基
をするアルキル化ビフエニル又はアルキル化ター
フエニルの少なくとも一つを単独もしくは他の溶
媒と併用したことを特徴とする感圧記録紙
(但し、アルキル化ビフエニルにおいてはアルキ
ル基の数は1〜4、アルキル化ターフエニルにお
いてはアルキル基の数は1〜6であり、2以上の
アルキル基は同一又は異なつてもよい。)
(特公昭49−21608)、
例えば
INDUSTRIAL APPLICATION FIELD The present invention relates to a dye solvent for pressure-sensitive recording paper, and more particularly to a mixture of p-isopropyl biphenyl, diisopropyl biphenyl and m-isopropyl biphenyl in a specific proportion, or a mixture of p-isopropyl biphenyl and diisopropyl biphenyl. A dye solvent for pressure-sensitive recording paper comprising a mixture of the following in a specific proportion. Prior art Pressure-sensitive recording paper develops color when a color former with electron-donating coloring reactivity is dissolved in an organic solvent, encapsulated in microcapsules, and brought into contact with a color former sheet coated on a support. It consists of a color developer sheet with a color developer coated on another support. In recent years, pressure sensitive recording paper has been widely used to replace carbon copy paper or pigment-type back carbon copy paper. Such pressure-sensitive recording paper must have excellent color development, long-term storage stability, and light resistance, and must also be low in toxicity and free from pollution problems. A solvent for dissolving the coloring agent (dye) in pressure-sensitive recording paper is required to meet the following requirements. (1) The color former has high solubility. (2) Do not cause any changes such as decomposition or color development of the coloring agent. (3) It has a fairly high boiling point and does not transpire during heat drying processes or at high temperatures. (4) It should not be eluted into water during encapsulation. (5) High color development speed and color density, and high color stability after color development. (6) Stable against light, heat and chemicals. (7) The viscosity should be low so that when the capsule is ruptured, the fluid can flow freely from inside the capsule. (8) Substantially free of odor. (9) It should be safe and have low toxicity to the human body. (10) Good biodegradability and no environmental pollution. The following solvents have been proposed as dye solvents for pressure-sensitive recording paper that meet these requirements. Pressure-sensitive recording paper characterized in that at least one of alkylated biphenyl or alkylated terphenyl having an alkyl group having 1 to 12 carbon atoms is used alone or in combination with other solvents as a solvent for the coloring agent (however, alkylated biphenyl (The number of alkyl groups is 1 to 4 in alkylated terphenyl, and the number of alkyl groups is 1 to 6 in alkylated terphenyl, and two or more alkyl groups may be the same or different.) (Japanese Patent Publication No. 49-21608), for example
【式】で示
されるイソプロピルビフエニル65%以上、ポリイ
ソプロピルビフエニル25%以下及びビフエニル10
%以下からなる溶剤に染料前駆体が溶解した溶剤
を内包したマイクロカプセルで被覆された記録シ
ート材料(特公昭54−37528)がある。
また、アルキルビフエニルの製造方法として
は、ビフエニルに対して、0.5〜10重量%のシリ
カ−アルミナ触媒又はゼオライト触媒もしくは両
者の混合触媒の存在下に、180℃以上の温度で、
ビフエニル1モルに対して0.5〜5モルの低級オ
レフインを接触させることを特徴とするm−、p
−位置換体に富むアルキルビフエニルの製造方法
(特公昭56−156222)が知られている。
特に、上述の特公昭54−37528の感圧記録紙用
染料溶剤の主たる構成成分であるイソプロピルビ
フエニルは次の構造式で示される化合物の異性体
混合物である。
(イソプロピル基はオルト、メタ又はパラ位置
でベンゼン環に付加される)。更に、特公昭54−
37528には、好適な感圧記録紙用染料溶剤の組成
が約50%m−イソプロピルビフエニル、30%p−
イソプロピルビフエニル、25%ポリイソプロピル
ビフエニル及び0.5%ビフエニルであると示され
ている。
また、市販されているイソプロピルビフエニル
及びビフエニルのフリーデルクラフツアルキル化
によつて合成される(Industrial and
Engineering Chemistry Product Reseach and
Development Vol.8,pp 239−241,1969)イソ
プロピルビフエニルはオルト−異性体を若干量含
有するメタ−異性体とパラ−異性体の混合物(メ
タ−異性体:パラ−:異性体(重量比)=約2:
1)である。
近年、記録紙の普及に伴い、感圧記録紙は、例
えば周囲温度が0℃以下の寒冷地での使用又は周
囲温度が約40〜50℃で相対湿度が約80%以上の高
温多湿の環境下での輸送及び長期間の保管の機会
が多くなつている。
特に、冬期ガソリンスタンド等の屋外施設にお
いては、0℃以下の低温の環境下で感圧記録紙が
使用される。このような低温環境下では、使用し
ている染料溶剤が結晶化してしまつたり、記録が
なされてから記録が明瞭に発現するまでの時間が
非常に長く、また発色したとしても書かれた記録
が判読できない程薄いので、実用に供し得ないと
いう問題が生じている。従つて、0℃においても
染料溶剤の結晶がほとんど生じない、且つ記録し
てから約30秒後の発色初期における発色率が少な
くとも40%である感圧記録用染料溶剤の提供が要
求されている。
更に、感圧記録紙の製造上及び保管上の見地か
ら臭いが実質的にない感圧記録紙用染料溶剤の提
供が切望されている。この臭気の問題は、感圧記
録紙の製造工程において、マイクロカプセルを支
持体の上に被覆した記録紙材料が乾燥後裁断され
る時に発生する。すなわち、記録紙材料が40〜50
℃の様な比較的高い温度で裁断された場合裁断に
よつて破壊されたマイクロカプセルから流出した
染料溶剤の臭いが作業者に不快感を与える。ま
た、裁断工程或いは製造時等において、衣服又は
手などに染料溶剤が付着することがある。付着し
た染料溶剤は、洗剤で洗つても、臭いが残り不快
感を与える。更に、記録済記録紙は比較的長期間
一箇所に集められて保管されるので、大量の記録
済記録紙から発する臭気が不快の原因となる。
このような臭気の問題を検討するに、上述の従
来提案されているイソプロピルビフエニルは臭気
がかなり強く感圧記録紙用染料溶剤としては好ま
しくない。このイソプロピルビフエニルはO−イ
ソプロピルビフエニル、m−イソプロピルビフエ
ニル及びp−イソプロピルビフエニルとの異性体
混合物、又は、m−イソプロピルビフエニルを主
成分とするp−イソプロピルビフエニルとの異性
体混合物である。O−イソプロピルビフエニルは
不快臭を示し、m−イソプロピルビフエニルもま
た臭気を有する。一方、p−イソプロピルビフエ
ニルはほとんど無臭で且つ染料溶解性も優れてい
るが、融点が比較的高いので、低温で結晶が析出
し易い欠点を有している。
従つて、ほとんど無臭で、低温下(例えば、0
℃)においても結晶がほとんど析出することのな
く且つ優れた初期発色性を示す感圧記録紙用染料
溶剤の提供が望まれている。
上述の要求される特性を有する感圧記録紙用染
料溶剤を提供する為、本発明者等の鋭意研究の結
果、p−イソプロピルビフエニル40〜75重量%、
ジイソプロピルビフエニル5〜40重量%及びm−
イソプロピルビフエニル20重量%以下の混合物又
はp−イソプロピルビフエニル60〜75重量%及び
ジイソプロピルビフエニル25〜40重量%の混合物
から成る溶剤がほとんど無臭で且つ低温下におい
ても結晶がほとんど析出することなく、更に前述
の感圧記録紙用染料溶剤の具備すべき条件をすべ
て満足するものであることを見い出し、この知見
に基づいて本発明を成すに至つた。
問題点を解決する手段
本発明の溶剤はp−イソプロピルビフエニル
(以下P−MIPBと略称す)40〜75量%ジイソプ
ロピルビフエニル(以下DIPBと略称す)5〜40
重量%及びm−イソプロピルビフエニル(以下m
−MIPBと略称す)20重量%以下からなる混合物
溶媒又はP−MIPB60〜75重量%及びDIPB25〜
40重量%からなる混合溶媒である。
本発明の感圧記録紙用染料溶剤の構成成分であ
るm−MIPB、p−MIPB及びDIPBの混合割合
は、図1に示す三角図の点A,B,C及びDで示
される範囲内である。
図1におけるAはm−MIPB20重量%、p−
MIPB75重量%及びDIPB5重量%の点であり、B
はm−MIPB0重量%、p−MIPB75重量%及び
DIPB25重量%の点であり、Cはm−MIPB0重量
%、p−MIPB60重量%及びDIPB40重量%の点
であり、且つDはm−MIPB20重量%、p−
MIPB40重量%及びDIPB40重量%の点である。
このような混合溶媒は、ほとんど無臭であり、
低温、例えば0℃でも結晶がほとんど析出するこ
とがなく且つ低温発色性、例えば−5℃での記録
してから30秒後の初期発色率が実質的な数値(40
%)以上であるので、感圧記録紙用染料溶剤とし
て有用なものである。
本発明の混合溶媒の好ましい混合割合は図1の
点a,b,c,dで示される範囲内で、aはm−
MIPB20重量%、p−MIPB70重量%及び
DIPB10重量%の点であり、bはm−MIPB0重量
%、p−MIPB70重量%、DIPB30重量%の点で
あり、cはm−MIPB0重量%、p−MIPB65重
量%及びDIPB35重量%の点であり、dはm−
MIPB20重量%、p−MIPB45重量%及び
DIPB35重量%の点である。
m−MIPBの含有量が20重量%を超えると、臭
気の点で問題を生ずるので好ましない。p−
MIPBの含有量が75重量%を超えると、低温で結
晶が析出し易くなるので好ましくない。また、
DIPBが40重量%を超えると、低温発色性が不充
分となり好ましくない。
本発明の混合溶媒の構成成分の一つである
DIPBは2,2′−、2,3′−2,4′−、3,3′−、
3,4′−、4,4′−等の異性体混合であるが、本
発明の効果はDIPBの異性体の種類によつて制限
されるものではない。
本発明の感圧記録紙用染料溶剤には、ほとんど
無臭であるという特性、優れた低温発色性及び低
温において結晶をほとんど析出しないという特性
をそこなわない限り、公知の感圧記録紙用染料溶
剤、例えばジイソプロピルナフタレン、水素化タ
ーフエニル及びブチルビフエニル、或いは感圧記
録紙用染料溶剤の希釈剤、例えばドデシルベンゼ
ン及びケロシンを混合し得る。
本発明の混合溶媒は、m−MIPB、P−
MTPB及びDIPBを上述の混合割合の範囲内で混
合して得ることも出来るし、また下記の方法によ
つて製造することもできる。
(1) ビフエニルとプロピレンを120〜260℃の温度
でシリカ−アルミナ触媒存在下で反応させてビ
フエニルのプロピル化を行ない、
得られた反応生成を減圧蒸留て5mmHgの減
圧下、平均沸点が138〜149℃の留分を分取する
ことから成る方法。
(2) ビフエニルとプロピレンを50〜90℃の温度で
塩化アルミニウム触媒の存在下で反応させてビ
フエニルのプロピル化を行ない、
得られた反応生成物を減圧蒸留でp−MIPB
を分離し精製し、又別途DIPBを蒸留分離精製
した後、精製したp−MIPBと所定の比率にな
るように混合することから成る方法。
シリカ−アルミナ触媒の存在下のビフエニルの
プロピル化の方法におけるシリカ−アルミナ触媒
としては、ナフタリン−ジイソプロピルナフタレ
ン混合物を280℃でトランスアルキル化する反応
において、
() 初期活性がナフタレン0.1Kg/Hr・Kg−触
媒、好ましくは0.2Kg/Hr・Kg−触媒以上であ
り、且つ
() 触媒重量の100倍のナフタレン−ジイソプ
ロピルナフタレン混合物を処理した後も、初期
活性の90%以上の活性を保持している、
シリカ−アルミナ触媒が好ましい。
上述のような特性を有するシリカ−アルミナ触
媒としては、日揮化学工業(株)製X−632NH及び
N−632Lを例示し得る。
プロピル化の反応温度は、120〜260℃、好まし
くは150〜240℃である。反応温度が120℃未満で
あると反応速度が遅く実用的でない。また反応温
度が260℃以上であると分解アルキル化反応が認
められ反応生成物が臭気を示すので好ましくな
い。
本発明の溶剤を使用する感圧記録紙は、感圧記
録紙用染料(発色剤)を溶解している、p−
MIPB40〜75重量%、DIPB5〜40重量%及びm−
MIPB20重量%以下の溶液又はp−MIPB60〜75
重量%及びDIPB5〜40重量%の溶剤を内包して
いるマイクロカプセルが塗布されて成ることを特
徴とする。従つて、カプセル化の方法、使用する
発色剤(染料)及び顕色剤、これらのスラリーの
調整方法、スラリーの塗布方法等に限定されるこ
となく、当業者に公知の方法は全て適用できる。
例えば、カプセル化の方法としては、米国特許
第2800457及び第2800458に開示のコアセルベーシ
ヨンを利用した方法、英国特許第990443及び米国
特許第3287154に開示されている界面重合による
方法等その他種々の方法が利用できる。
発色剤(染料)としては、トリフエニルメタン
系化合物、ジフエニルメタン系化合物、キサンテ
ン系化合物、チアジン系化合物、スピロピラン系
化合物等を例示し得る。更に、顕色剤として用い
られる酸性物質としては、酸性白土、活性白土、
アタパルシヤイト、ベントナイト、ゼオライト等
のような活性粘土物質或いは、フエノール樹脂、
酸反応性フエノール−ホルムアルデヒドノボラツ
ク樹脂、芳香族有機酸の金属等のような有機酸性
物質等を例示し得る。
発明の効果
本発明の感圧記録紙用染料溶剤は、ほとんど無
臭であり、染料の溶解性に優れ、且つ低温(0
℃)においてその結晶がほとんど析出せず、且つ
前述の感圧記録紙用染料溶剤の具備すべき必要条
件を満足するものである。更に、本発明の溶剤を
使用する感圧記録紙は低温(−5℃)における記
録してから30秒後の初期発色率が40%以上で、寒
冷地においても充分実用に供し得るものである。
以下実施例により本発明を具体的に説明するが
本発明は実施例に限定されるものではない。
[触媒活性測定法]
装 置
内径約25mmのステンレススチール製反応管の下
部に触媒を支持するための2mmφのガラスビーズ
10mlを充填し、その上部に触媒25mlを充填する。
さらにその上に予熱ゾーンとして2mmφのガラス
ビーズ20mlを充填する。加熱は外部から電熱器で
行ない反応管中に挿入した熱電対で温度を測定す
る。
方 法
ナフタレンとジイソプロピルナフタレン(異性
体混合物)との等モル混合物を約60℃に加熱し
て、ナフタレンを溶解させる。反応器上部よりこ
の混合物を一定の流量で供給し、触媒層を280℃
に維持して連続的にナフタレンとジイソプロピル
ナフタレンを反応させる。反応管下部から流出す
る反応液は100℃以下に冷却し、必要に応じてサ
ンプリングしガスクロマトグラフイーで分析す
る。流量は、ナフタレンの初期反応率が10〜20%
になるように設定する。また原料のナフタレンと
ジイソプロピルナフタレンはイオウや窒素化合物
等触媒活性を損う成分の少ないものを使用する。
評 価
反応開始から触媒重量の約5倍のナフタリン−
ジイソプロピルナフタレン混合物を反応させた時
点の生成物の分析結果からナフタレンの転化率
(X0)を求め、次の式にて触媒の初期活性を求め
る。
初期活性(A0)=(WN)×(X0)/(WC)
(式中、WCは触媒充填量(g)を示し、WNはナ
フタレン供給速度(g/Hr)を示す。)
引き続き反応を継続し、触媒重量の100倍のナ
フタレン−ジイソプロピルナフタレン混合物を反
応させた時点でのナフタレンの転化率(X100)を
生成物の分析結果から求め、次の式にて触媒活性
の保持率を求める。
活性保持率(Ap)=(X100)/(X0)×100
触媒の活性試験例
シリカアルミナ触媒[日揮化学工業(株)製X−
632HN(3mmφペレツト)]25gを反応管に充填
し、ナフタレン−ジイソプロピルナフタレンの等
モル混合物を250ml/Hr.(245g/Hr.)で供給
し、280℃でトランスアルキル化反応をおこなつ
た。
反応開始後、30分後及び10時間後の反応液を捕
集し、ガスクロマトグラフ分析をおこなつた。
その結果は以下の通りである。
X0 =17.0%
X100=16.2%
AP=95.3%
また初期活性は、WN=92.2g/Hr.及び WC
=25gから次の通りである。
A0=92.2×0.17/25=0.63Kg/Hr.Kg−触媒
実施例 1
容量1.5のステンレス製オートクレーブにビ
フエニル1000gと触媒の活性試験例で用いたシリ
カアルミナ触媒(日揮化学工業(株)製、X−
632HN)100gを仕込み、加熱して反応器内温度
を70℃以上としビフエニルを溶融させた。次いで
撹拌を開始し、更に加熱して反応器内温度を240
℃とした。ボンベよりプロピレンガスを導入し、
圧力を約2Kg/cm2・Gに維持し、240℃でプロピ
ル化反応を行なつた。反応中、時々反応液を採取
して組成を分析し、平均プロピル化度がおよそ
1.0となつた時点でプロピレンガスの供給を停止
した。冷却して回収した反応液の組成は以下の通
りである。
表−1成 分 組成(mol%)
ビフエニル 27.8
o−イソプロピルビフエニル(O−MIPB)
6.0
m−MIPB 18.7
p−MIPB 22.1
DIPB 23.9
トリイソプロピルビフエニル他(TIPB) 1.5
かようにして得られた反応生成物を5mmHgの
減圧下、140℃で注意深く分留した。得られた留
分の組成は次の通りである。
表−2成 分 組成(重量%)
m−MIPB 15.0
p−MIPB 71.9DIPB 13.1
比較例 1
実施例1と同様にしてビフエニルのプロピル化
反応を行なつた。得られた反応生成物を5mmHg
の減圧下141〜150℃で分留した。得られた留分の
組成は次の通りである。
表−3成 分 組成(重量%)
m−PIPB 0.8
p−MIPB 47.6DIPB 51.6
実施例2〜4及び比較例2
実施例1と同様のシリカアルミナ触媒及び同様
の方法を用い、表−4に示す反応温度でビフエニ
ルのプロピル化反応を行つた。得られた反応生成
物を実施例1と同様の方法で蒸留してp−MIPB
を主成分とする留分を得た。
反応生成物の組成及び留分の組成を表−4に示
す。65% or more of isopropyl biphenyl, 25% or less of polyisopropyl biphenyl and biphenyl 10 represented by [formula]
There is a recording sheet material (Japanese Patent Publication No. 37528/1983) coated with microcapsules containing a dye precursor dissolved in a solvent containing a dye precursor of less than 1%. In addition, as a method for producing alkyl biphenyl, in the presence of 0.5 to 10% by weight of a silica-alumina catalyst, a zeolite catalyst, or a mixed catalyst of both based on biphenyl, at a temperature of 180 ° C. or higher,
m-, p characterized in that 0.5 to 5 mol of lower olefin is brought into contact with 1 mol of biphenyl.
A method for producing alkyl biphenyl rich in substituents at the -position (Japanese Patent Publication No. 56-156222) is known. In particular, isopropylbiphenyl, which is the main constituent of the dye solvent for pressure-sensitive recording paper disclosed in Japanese Patent Publication No. 54-37528, is an isomer mixture of compounds represented by the following structural formula. (The isopropyl group is attached to the benzene ring in the ortho, meta or para position). In addition, the special public service 1977-
37528, the composition of a suitable dye solvent for pressure-sensitive recording paper is approximately 50% m-isopropyl biphenyl, 30% p-
Isopropylbiphenyl, 25% polyisopropylbiphenyl and 0.5% biphenyl. It is also synthesized by commercially available isopropyl biphenyl and Friedel-Crafts alkylation of biphenyl (Industrial and
Engineering Chemistry Product Research and
Development Vol. 8, pp 239-241, 1969) Isopropylbiphenyl is a mixture of meta and para isomers (meta: para: isomers (weight ratio ) = approx. 2:
1). In recent years, with the spread of recording paper, pressure-sensitive recording paper can be used, for example, in cold regions where the ambient temperature is below 0°C, or in hot and humid environments where the ambient temperature is approximately 40 to 50°C and the relative humidity is approximately 80% or higher. There are many opportunities for underground transportation and long-term storage. Particularly, pressure-sensitive recording paper is used in outdoor facilities such as winter gas stations in environments with low temperatures of 0° C. or lower. In such a low-temperature environment, the dye solvent used may crystallize, the time from when a record is made until the record clearly appears is extremely long, and even if color develops, the written record may The problem has arisen that it cannot be put to practical use because it is so thin that it cannot be read. Therefore, there is a need to provide a dye solvent for pressure-sensitive recording in which almost no crystals of the dye solvent occur even at 0° C., and which has a color development rate of at least 40% at the initial stage of color development approximately 30 seconds after recording. . Furthermore, from the viewpoint of manufacturing and storage of pressure-sensitive recording paper, it is strongly desired to provide a dye solvent for pressure-sensitive recording paper that is substantially odorless. This odor problem occurs during the manufacturing process of pressure-sensitive recording paper, when recording paper material coated with microcapsules on a support is dried and then cut. That is, the recording paper material is 40 to 50
When cutting is carried out at a relatively high temperature such as ℃, the odor of the dye solvent flowing out from the microcapsules destroyed by cutting gives an unpleasant feeling to the operator. Furthermore, during the cutting process or manufacturing process, the dye solvent may adhere to clothes or hands. Even if the attached dye solvent is washed with detergent, the odor remains and causes discomfort. Furthermore, since the recorded paper is collected and stored in one place for a relatively long period of time, the odor emitted from the large amount of recorded paper can cause discomfort. Considering the problem of odor, the above-mentioned conventionally proposed isopropyl biphenyl has a rather strong odor and is not suitable as a dye solvent for pressure-sensitive recording paper. This isopropylbiphenyl is an isomer mixture with O-isopropylbiphenyl, m-isopropylbiphenyl and p-isopropylbiphenyl, or an isomer mixture with p-isopropylbiphenyl whose main component is m-isopropylbiphenyl. It is. O-isopropylbiphenyl exhibits an unpleasant odor, and m-isopropylbiphenyl also has an odor. On the other hand, although p-isopropylbiphenyl is almost odorless and has excellent dye solubility, it has a relatively high melting point, so it has the disadvantage that crystals tend to precipitate at low temperatures. Therefore, it is almost odorless and can be used at low temperatures (e.g. 0
It is desired to provide a dye solvent for pressure-sensitive recording paper that exhibits excellent initial color development and hardly precipitates crystals even at temperatures (°C). In order to provide a dye solvent for pressure-sensitive recording paper having the above-mentioned required properties, as a result of intensive research by the present inventors, 40 to 75% by weight of p-isopropylbiphenyl,
5-40% by weight of diisopropylbiphenyl and m-
A solvent consisting of a mixture of 20% by weight or less of isopropylbiphenyl or a mixture of 60 to 75% by weight of p-isopropylbiphenyl and 25 to 40% by weight of diisopropylbiphenyl is almost odorless and hardly precipitates crystals even at low temperatures. Furthermore, it was discovered that the dye solvent for pressure-sensitive recording paper satisfies all of the above-mentioned conditions, and based on this knowledge, the present invention was accomplished. Means for Solving the Problems The solvent of the present invention contains 40 to 75% p-isopropyl biphenyl (hereinafter abbreviated as P-MIPB) and 5 to 40% diisopropyl biphenyl (hereinafter abbreviated as DIPB).
Weight% and m-isopropylbiphenyl (hereinafter m
- A mixture of solvents consisting of 20% by weight or less (abbreviated as MIPB) or P-MIPB60 to 75% by weight and DIPB25 to
It is a mixed solvent consisting of 40% by weight. The mixing ratio of m-MIPB, p-MIPB, and DIPB, which are the constituent components of the dye solvent for pressure-sensitive recording paper of the present invention, is within the range shown by points A, B, C, and D in the triangular diagram shown in FIG. be. A in Figure 1 is m-MIPB 20% by weight, p-
It is a point of 75% by weight of MIPB and 5% by weight of DIPB, and B
m-MIPB 0% by weight, p-MIPB 75% by weight and
DIPB25 wt% point, C is m-MIPB0 wt%, p-MIPB60 wt% and DIPB40 wt% point, and D is m-MIPB20 wt%, p-MIPB20 wt% point.
The points are 40% by weight of MIPB and 40% by weight of DIPB. Such mixed solvents are almost odorless,
Almost no crystals precipitate even at low temperatures, for example 0℃, and low-temperature color development, for example, the initial color development rate 30 seconds after recording at -5℃ is a substantial value (40℃).
%), it is useful as a dye solvent for pressure-sensitive recording paper. The preferred mixing ratio of the mixed solvent of the present invention is within the range shown by points a, b, c, and d in Figure 1, where a is m-
MIPB 20% by weight, p-MIPB 70% by weight and
b is the point of DIPB 10% by weight, b is the point of m-MIPB 0% by weight, p-MIPB 70% by weight, DIPB 30% by weight, c is the point of m-MIPB 0% by weight, p-MIPB 65% by weight and DIPB 35% by weight. Yes, d is m-
MIPB 20% by weight, p-MIPB 45% by weight and
The point is DIPB 35% by weight. If the content of m-MIPB exceeds 20% by weight, it is not preferred because it causes problems in terms of odor. p-
If the content of MIPB exceeds 75% by weight, crystals tend to precipitate at low temperatures, which is not preferable. Also,
If DIPB exceeds 40% by weight, low-temperature color development becomes insufficient, which is not preferable. It is one of the constituent components of the mixed solvent of the present invention.
DIPB is 2,2'-, 2,3'-2,4'-, 3,3'-,
Although it is a mixture of isomers such as 3,4'- and 4,4'-, the effects of the present invention are not limited by the type of isomer of DIPB. The dye solvent for pressure-sensitive recording paper of the present invention may be any of the known dye solvents for pressure-sensitive recording paper, as long as it does not impair the properties of being almost odorless, excellent low-temperature color development, and hardly precipitating crystals at low temperatures. , for example diisopropylnaphthalene, hydrogenated terphenyl and butyl biphenyl, or diluents of dye solvents for pressure-sensitive recording paper, such as dodecylbenzene and kerosene. The mixed solvent of the present invention includes m-MIPB, P-
It can be obtained by mixing MTPB and DIPB within the above mixing ratio range, or it can also be produced by the method below. (1) Biphenyl and propylene are reacted at a temperature of 120 to 260°C in the presence of a silica-alumina catalyst to propylate biphenyl, and the resulting reaction product is distilled under reduced pressure to give an average boiling point of 138 to 138. A method consisting of separating the fraction at 149°C. (2) Biphenyl is propylated by reacting biphenyl and propylene at a temperature of 50 to 90°C in the presence of an aluminum chloride catalyst, and the resulting reaction product is distilled under reduced pressure to produce p-MIPB.
A method consisting of separating and purifying DIPB, and separately distilling and purifying DIPB, and then mixing it with purified p-MIPB at a predetermined ratio. In the process of propylating biphenyl in the presence of a silica-alumina catalyst, the silica-alumina catalyst is used in the transalkylation of a naphthalene-diisopropylnaphthalene mixture at 280°C. - Catalyst, preferably 0.2 Kg/Hr.Kg - Catalyst, and () retains 90% or more of its initial activity even after treatment with a naphthalene-diisopropylnaphthalene mixture 100 times the weight of the catalyst. , silica-alumina catalysts are preferred. Examples of the silica-alumina catalyst having the above characteristics include X-632NH and N-632L manufactured by JGC Chemical Industries, Ltd. The reaction temperature for propylation is 120-260°C, preferably 150-240°C. If the reaction temperature is less than 120°C, the reaction rate is too slow to be practical. Further, if the reaction temperature is 260° C. or higher, a decomposition alkylation reaction is observed and the reaction product exhibits an odor, which is not preferable. The pressure-sensitive recording paper using the solvent of the present invention is a p-
MIPB40-75% by weight, DIPB5-40% by weight and m-
MIPB20wt% or less solution or p-MIPB60-75
It is characterized by being coated with microcapsules containing a solvent of 5 to 40% by weight and DIPB. Therefore, any methods known to those skilled in the art can be applied without being limited to the encapsulation method, the color forming agent (dye) and color developer used, the method of preparing slurry thereof, the method of applying the slurry, etc. For example, various encapsulation methods include a method using coacelvation disclosed in U.S. Patent No. 2800457 and No. 2800458, a method using interfacial polymerization disclosed in British Patent No. 990443 and U.S. Patent No. 3287154, etc. methods are available. Examples of the coloring agent (dye) include triphenylmethane compounds, diphenylmethane compounds, xanthene compounds, thiazine compounds, and spiropyran compounds. Furthermore, acidic substances used as color developers include acid clay, activated clay,
activated clay materials such as attaparsiaite, bentonite, zeolite etc. or phenolic resins,
Examples include organic acidic substances such as acid-reactive phenol-formaldehyde novolac resins, metals of aromatic organic acids, and the like. Effects of the Invention The dye solvent for pressure-sensitive recording paper of the present invention is almost odorless, has excellent dye solubility, and can be used at low temperatures (0.
C), the crystals hardly precipitate, and the above-mentioned requirements for a dye solvent for pressure-sensitive recording paper are satisfied. Furthermore, the pressure-sensitive recording paper using the solvent of the present invention has an initial color development rate of 40% or more 30 seconds after recording at a low temperature (-5°C), and can be used practically even in cold regions. . EXAMPLES The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to the Examples. [Catalytic activity measurement method] Apparatus: Glass beads with a diameter of 2 mm to support the catalyst at the bottom of a stainless steel reaction tube with an inner diameter of approximately 25 mm.
Fill with 10 ml and fill with 25 ml of catalyst on top.
Furthermore, 20 ml of 2 mm diameter glass beads are filled on top of it as a preheating zone. Heating is performed externally with an electric heater, and the temperature is measured with a thermocouple inserted into the reaction tube. Method An equimolar mixture of naphthalene and diisopropylnaphthalene (mixture of isomers) is heated to approximately 60°C to dissolve the naphthalene. This mixture is supplied from the top of the reactor at a constant flow rate, and the catalyst layer is heated to 280℃.
to continuously react naphthalene and diisopropylnaphthalene. The reaction liquid flowing out from the bottom of the reaction tube is cooled to below 100°C, and if necessary, sampled and analyzed by gas chromatography. The flow rate is such that the initial reaction rate of naphthalene is 10-20%
Set it so that In addition, the naphthalene and diisopropylnaphthalene used as raw materials are those containing few components that impair catalyst activity, such as sulfur and nitrogen compounds. Evaluation Approximately 5 times the weight of the catalyst was naphthalene from the start of the reaction.
The naphthalene conversion rate (X 0 ) is determined from the analysis results of the product at the time when the diisopropylnaphthalene mixture is reacted, and the initial activity of the catalyst is determined using the following equation. Initial activity (A 0 ) = (W N ) × (X 0 )/(W C ) (where, W C indicates the catalyst loading amount (g), and W N indicates the naphthalene supply rate (g/Hr). ) Continuing the reaction, the conversion rate of naphthalene (X 100 ) at the time when 100 times the weight of the catalyst was reacted with the naphthalene conversion rate (X 100 ) was determined from the analysis results of the product, and the catalyst activity was calculated using the following formula. Find the retention rate. Activity retention rate (Ap) = (X 100 ) / (X 0 ) × 100 Catalyst activity test example Silica alumina catalyst [X-
632HN (3 mmφ pellets)] was filled into a reaction tube, and an equimolar mixture of naphthalene-diisopropylnaphthalene was supplied at 250 ml/Hr. (245 g/Hr.) to carry out a transalkylation reaction at 280°C. The reaction solution was collected 30 minutes and 10 hours after the start of the reaction, and analyzed by gas chromatography. The results are as follows. X 0 = 17.0% X 100 = 16.2% A P = 95.3% Also, the initial activity is W N = 92.2 g/Hr .
From =25g, it is as follows. A 0 = 92.2 x 0.17/25 = 0.63 Kg/Hr.Kg - Catalyst Example 1 In a stainless steel autoclave with a capacity of 1.5, 1000 g of biphenyl and the silica alumina catalyst used in the catalyst activity test example (manufactured by JGC Chemical Co., Ltd., X-
632HN) was charged and heated to raise the temperature inside the reactor to 70°C or higher to melt the biphenyl. Next, start stirring and further heat to bring the temperature inside the reactor to 240°C.
℃. Introducing propylene gas from a cylinder,
The pressure was maintained at about 2 Kg/cm 2 ·G, and the propylation reaction was carried out at 240°C. During the reaction, the reaction solution was sampled from time to time to analyze its composition, and the average degree of propylation was approximately
Propylene gas supply was stopped when it reached 1.0. The composition of the cooled and collected reaction solution is as follows. Table-1 Ingredients Composition (mol%) Biphenyl 27.8 o-isopropylbiphenyl (O-MIPB)
6.0 m-MIPB 18.7 p-MIPB 22.1 DIPB 23.9 Triisopropylbiphenyl, etc. (TIPB) 1.5 The reaction product thus obtained was carefully fractionated at 140°C under a reduced pressure of 5 mmHg. The composition of the obtained fraction is as follows. Table 2 Components Composition (% by weight) m-MIPB 15.0 p-MIPB 71.9 DIPB 13.1 Comparative Example 1 A propylation reaction of biphenyl was carried out in the same manner as in Example 1. The obtained reaction product was heated to 5 mmHg.
Fractional distillation was carried out at 141-150°C under reduced pressure. The composition of the obtained fraction is as follows. Table 3 Components Composition (wt%) m-PIPB 0.8 p-MIPB 47.6 DIPB 51.6 Examples 2 to 4 and Comparative Example 2 Using the same silica alumina catalyst and the same method as in Example 1, the compounds shown in Table 4 were The propylation reaction of biphenyl was carried out at the reaction temperature. The obtained reaction product was distilled in the same manner as in Example 1 to obtain p-MIPB.
A fraction containing as the main component was obtained. Table 4 shows the composition of the reaction product and the fraction.
【表】
比較例 3
(塩化アルムニウム触媒による反応)
容量1のガラス製オートクレーブにビフエニ
ル500gを仕込み、反応器内温度を80℃に昇温し
て融解する。次いで触媒として無水塩化アルミニ
ウム14gを添加した後、オートクレーブを密閉し
て撹拌を開始した。ボンべによりプロピレンを導
入し、反応器温度を100〜110℃、圧力を約1Kg/
cm2・Gに維持し、平均アルキル化度が約1となる
迄反応を継続した。反応終了後、反応生成物を塩
酸及び純水で充分洗浄し、触媒を除去した。かよ
うに処理された反応生成物を精密蒸留塔で注意深
く分留すた。得られた反応生成物及び留分の組成
は下記の通りである。[Table] Comparative Example 3 (Reaction using aluminum chloride catalyst) 500 g of biphenyl was charged into a glass autoclave with a capacity of 1, and the temperature inside the reactor was raised to 80°C to melt it. Next, after adding 14 g of anhydrous aluminum chloride as a catalyst, the autoclave was sealed and stirring was started. Introduce propylene using a cylinder, adjust the reactor temperature to 100-110℃, and increase the pressure to approximately 1Kg/kg.
cm 2 ·G, and the reaction was continued until the average degree of alkylation was approximately 1. After the reaction was completed, the reaction product was thoroughly washed with hydrochloric acid and pure water to remove the catalyst. The reaction product thus treated was carefully fractionated using a precision distillation column. The compositions of the obtained reaction product and fraction are as follows.
【表】
実施例 5
(感圧記録紙用染料溶液の調製)
実施例1によつて得られた溶剤100mlを150℃に
加温し、撹拌下にCVL(保土ケ谷化学工業(株)製青
染料)30gを溶解した。
次いでこの溶液を20℃の恒温槽内に入れ放置
し、経済的に溶液中のCVLの濃度を測定した。
その結果を次の表に示す。表−6より極めて高濃
度の状態を長期間安定に保持することが明確であ
る。
表−6経過時間 1日目 7日目 14日目
溶液中染料濃度 19.6 13.9 10.8(g/100ml)
実施例 6
マイクロカプセルの調製
実施例5で得られた感圧記録紙用染料溶剤を用
いマイクロカプセルを以下の方法で調製する。
メラミン630gと2%NaOH水溶液でPH=9.0に
調整したホルマリン(37%ホルムアルデヒド水溶
液。以下同じ。)1620gを混合し70℃に加熱した。
メラミンが溶解したら直ちに水2250gを加えてそ
のまま3分間撹拌してメラミンホルムアルデヒド
プレポリマー水溶液を得た。
トリエタノールアミンでPH=8.5に調整したホ
ルマリン1460gと尿素600gを混合し、70℃で1
時間反応させて尿素ホルムアルデヒドプレポリマ
ー水溶液を得た。
37%ホルムアルデヒド水溶液1620gと尿素600
gを混合撹拌し、この混合物にトリエタノールア
ミンを加えてPH=8.8に調整した後、温度70℃で
30分間反応させた。
この反応混合物400gをとりこれに水24gとテ
トラエチレンペンタミン30gを加え、温度70℃で
撹拌しながら15℃塩酸でPHを3に調整した。反応
の経過とともにPHが低下するので反応混合物に10
%カセイソーダ水溶液を加えてそのPHを3に調整
しなおし、温度を55℃に下げて反応を続けた。反
応混合物の粘度が200cpsとなつた時点で10%カセ
イソーダ水溶液で中和し、水4000gを加え水溶液
性カチオニツク尿素樹脂の水溶液を得た。
メラミンプレポリマー1000g、尿素プレポレマ
ー500g、上述のカチオニツク尿素樹脂1580g、
水620g及びトリエタノールアミン10gの混合液
を10%クエン酸水溶液でPH=5.2に調整した後、
10%ネオベレツクス水溶液(花王アトラス(株)製界
面活性剤)30gを加えA液とした。
別にCVL(保土ケ谷化学工業(株)製青染料)500
gを9500gの実施例1の溶剤に溶解しB液とし
た。A液中にB液1000mlをホモジナイザーで粒径
が2〜8μmになる様に乳化させ、その後ゆつく
り撹拌しながら温度を30℃に保ち1%クエン酸水
溶液を加えてPH=3.6にした。その後この乳化液
を1時間撹拌した後、2000mlの水を加えた。さら
に3時間経過後20%クエン酸を加えてPH=3.0に
して20時間撹拌を続けてマイクロカプセルスラリ
ーを得た。
感圧記録紙の調製
かようにして得られたマイクロカプセル300g
を、別に調整したPVA(クラレ(株)製ポリビニルア
ルコール)の10%溶液600mlに加えよく撹拌し分
散液を得た。この分散液を45g/m2の坪量の紙に
マイクロカプセルの塗布量が22g/m2になる様に
塗布した。これをパラフエニルフイエノールとホ
ルムアルデヒドの縮合物を主顕色剤とする顕色性
物質を、常法により塗布した顕色紙と組み合わせ
て感圧記録紙を得た。
得られた感圧記録紙を通常の環境下でオリベツ
テイー社製のタイプライターで発色し、暗所に24
時間保存した後MacBeth社製の反射色温度計で
発色濃度を測定した。
一方、同じ感圧複写紙を−5℃の環境下で同様
に発色し、発色直後からの濃度の変化を同じく反
射色度計で測定し、常温で24時間保存した結果を
100とした時の各経過時間に於ける相対発色率を
求めた。その結果を表−7に示す。表−7から、
この感圧記録紙は30秒の様な初期時点においても
十分な発色性能を示している。
表−7経過時間 30秒 1分 1時間 発色率 70% 77% 88%
実施例 7
実施例2〜4及び比較例1で得られた溶媒を用
いて実施例6の方法によつて感圧記録紙を調製し
た。
得られた感圧記録紙の初期発色性(−5℃で記
録後30秒経過時点の発生性能)は次の通りであ
る。
表−8 実施例2 実施例3 実施例4 比較例1
発色率 57 62 72 25 (%)
試験例 1
実施例1〜4及び比較例2〜3で得られた溶媒
について無作為に選択した男・女各20人により臭
気に関するパネルテストをおこなつた。[Table] Example 5 (Preparation of dye solution for pressure-sensitive recording paper) 100 ml of the solvent obtained in Example 1 was heated to 150°C, and while stirring, CVL (blue dye manufactured by Hodogaya Chemical Industry Co., Ltd.) was added. ) 30g was dissolved. Next, this solution was placed in a constant temperature bath at 20°C and left to stand, and the concentration of CVL in the solution was measured economically.
The results are shown in the table below. From Table 6, it is clear that the extremely high concentration state can be stably maintained for a long period of time. Table 6 Elapsed time 1st day 7th day 14th day Dye concentration in solution 19.6 13.9 10.8 (g/100ml) Example 6 Preparation of microcapsules Using the dye solvent for pressure-sensitive recording paper obtained in Example 5, Capsules are prepared in the following manner. 630 g of melamine and 1620 g of formalin (37% formaldehyde aqueous solution; the same applies hereinafter) adjusted to pH=9.0 with a 2% NaOH aqueous solution were mixed and heated to 70°C.
Immediately after the melamine was dissolved, 2250 g of water was added and the mixture was stirred for 3 minutes to obtain a melamine formaldehyde prepolymer aqueous solution. Mix 1,460 g of formalin adjusted to pH=8.5 with triethanolamine and 600 g of urea, and heat at 70°C.
A urea formaldehyde prepolymer aqueous solution was obtained by reacting for a period of time. 1620g of 37% formaldehyde aqueous solution and 600g of urea
After stirring, adding triethanolamine to the mixture and adjusting the pH to 8.8, the mixture was heated to 70°C.
The reaction was allowed to proceed for 30 minutes. 400g of this reaction mixture was taken, 24g of water and 30g of tetraethylenepentamine were added thereto, and the pH was adjusted to 3 with hydrochloric acid at 15°C while stirring at a temperature of 70°C. 10 in the reaction mixture as the pH decreases as the reaction progresses.
% caustic soda aqueous solution was added to adjust the pH to 3, the temperature was lowered to 55°C, and the reaction was continued. When the viscosity of the reaction mixture reached 200 cps, it was neutralized with a 10% caustic soda aqueous solution, and 4000 g of water was added to obtain an aqueous solution of an aqueous cationic urea resin. 1000 g of melamine prepolymer, 500 g of urea prepolymer, 1580 g of the above-mentioned cationic urea resin,
After adjusting the mixed solution of 620 g of water and 10 g of triethanolamine to PH = 5.2 with a 10% aqueous citric acid solution,
30 g of a 10% Neoberex aqueous solution (surfactant manufactured by Kao Atlas Co., Ltd.) was added to prepare Solution A. Separately CVL (Blue dye manufactured by Hodogaya Chemical Industry Co., Ltd.) 500
g was dissolved in 9,500 g of the solvent of Example 1 to obtain liquid B. 1000 ml of Solution B was emulsified in Solution A using a homogenizer so that the particle size was 2 to 8 μm, and then a 1% aqueous citric acid solution was added to the emulsion with gentle stirring while maintaining the temperature at 30° C. to adjust the pH to 3.6. After this emulsion was stirred for 1 hour, 2000 ml of water was added. After a further 3 hours, 20% citric acid was added to adjust the pH to 3.0 and stirring was continued for 20 hours to obtain a microcapsule slurry. Preparation of pressure sensitive recording paper 300g of microcapsules thus obtained
was added to 600 ml of a separately prepared 10% solution of PVA (polyvinyl alcohol manufactured by Kuraray Co., Ltd.) and stirred thoroughly to obtain a dispersion. This dispersion was applied to paper with a basis weight of 45 g/m 2 so that the amount of microcapsules coated was 22 g/m 2 . This was combined with a color developer paper coated with a color developer material containing a condensate of paraphenylphyenol and formaldehyde as the main color developer by a conventional method to obtain a pressure-sensitive recording paper. The resulting pressure-sensitive recording paper was colored using an Olivetsu Typewriter under normal conditions, and then left in a dark place for 24 hours.
After storage for a period of time, the color density was measured using a reflective color thermometer manufactured by MacBeth. On the other hand, the same pressure-sensitive copying paper was colored in the same way in an environment of -5℃, the change in density immediately after coloring was measured using the same reflection colorimeter, and the results were stored at room temperature for 24 hours.
The relative color development rate at each elapsed time was determined when it was set as 100. The results are shown in Table-7. From Table-7,
This pressure-sensitive recording paper shows sufficient color development performance even at an initial time of 30 seconds. Table 7 Elapsed time 30 seconds 1 minute 1 hour Color development rate 70% 77% 88% Example 7 Pressure-sensitive recording by the method of Example 6 using the solvents obtained in Examples 2 to 4 and Comparative Example 1 A paper was prepared. The initial color development performance (development performance after 30 seconds of recording at -5°C) of the pressure-sensitive recording paper obtained is as follows. Table 8 Example 2 Example 3 Example 4 Comparative Example 1 Color development rate 57 62 72 25 (%) Test Example 1 Randomly selected man for the solvents obtained in Examples 1 to 4 and Comparative Examples 2 to 3・A panel test regarding odor was conducted by 20 women each.
【表】
実用に供し得る感圧記録紙用染料溶剤として
は、評価B以上であることが必要である。
試験例 2
実施例1〜4及び比較例2〜3で得られた溶媒
について5℃及び0℃の恒温槽で24時間保ち、結
晶析出の有無を調べた。
結果を表−10に示す。[Table] A practically usable dye solvent for pressure-sensitive recording paper must have a rating of B or higher. Test Example 2 The solvents obtained in Examples 1 to 4 and Comparative Examples 2 to 3 were kept in constant temperature baths at 5°C and 0°C for 24 hours, and the presence or absence of crystal precipitation was examined. The results are shown in Table-10.
【表】
実用に供し得る感圧記録紙用染料溶剤としては
評価B以上であることが必要である。
実施例 8
容量1のガラス製オートクレーブにビフエニ
ル500gを仕込み、反応器内の温度を80℃に昇温
して融解する。次いで触媒として無水塩化アルミ
ニウム14gを添加した後、オートクレーブを密閉
して撹拌を開始した。ボンべよりプロピレンを導
入し、反応器内温度を100〜110℃、圧力を約1
Kg/cm2・Gに維持し、平均アルキル化度が約1と
なるまで反応を継続した。反応終了後、反応物を
塩酸及び水で洗浄し、触媒を除去した。この様に
して得られた反応液を減圧精密蒸留塔で蒸留し、
純度が92%のp−MIPB約120gを分離し、続い
てジヤケツト付きのガラス容器で撹拌下に12℃に
冷却し、得られたスラリーを遠心分離器にかけて
純度99%のp−MIPBを分離した。
一方、蒸留で反応得よりp−MIPB8重量%、
DIPB92重量%の混合物を26g分離し、晶析で得
られた純度99%のp−MIPBと混合しp−
MIPB73.2重量%、DIPB26.8重量%の混合溶液を
得た。この混合溶液を用いた感圧紙を実施例5〜
6に示す方法により調整し、実施例7に示す方法
により性能を比較した。
その結果;−5℃/30秒における発色濃度59%
臭 気 B
結晶析出 5℃ A
0℃ A[Table] A practically usable dye solvent for pressure-sensitive recording paper must be rated B or higher. Example 8 500 g of biphenyl was charged into a glass autoclave with a capacity of 1, and the temperature inside the reactor was raised to 80° C. to melt it. Next, after adding 14 g of anhydrous aluminum chloride as a catalyst, the autoclave was sealed and stirring was started. Introduce propylene from the cylinder, raise the temperature inside the reactor to 100-110℃, and increase the pressure to about 1
Kg/cm 2 ·G was maintained, and the reaction was continued until the average degree of alkylation was approximately 1. After the reaction was completed, the reaction product was washed with hydrochloric acid and water to remove the catalyst. The reaction solution obtained in this way was distilled in a vacuum precision distillation column,
Approximately 120 g of p-MIPB with a purity of 92% was separated, then cooled to 12°C with stirring in a glass container with a jacket, and the resulting slurry was centrifuged to separate p-MIPB with a purity of 99%. . On the other hand, 8% by weight of p-MIPB was obtained from the reaction product by distillation.
26g of 92% by weight DIPB mixture was separated, mixed with 99% pure p-MIPB obtained by crystallization, and p-
A mixed solution containing 73.2% by weight of MIPB and 26.8% by weight of DIPB was obtained. Pressure-sensitive paper using this mixed solution was prepared in Examples 5-
It was prepared by the method shown in Example 6, and the performance was compared by the method shown in Example 7. Result: Color density 59% at -5°C/30 seconds Odor B Crystal precipitation 5°C A 0°C A
図1は、m−MIPB、p−MIPB及びDIPBの
含有割合を示した三角図である。
FIG. 1 is a triangular diagram showing the content ratios of m-MIPB, p-MIPB and DIPB.
Claims (1)
ジイソプロピルビフエニル5〜40重量%及びm−
イソプロピルビフエニル20重量%以下からなる感
圧記録紙用染料溶剤。 2 p−イソプロピルビフエニル60〜75重量%及
びジイソプロピルビフエニル25〜40重量%とから
なる感圧記録紙用染料溶剤。[Claims] 1 40 to 75% by weight of p-isopropylbiphenyl,
5-40% by weight of diisopropylbiphenyl and m-
A dye solvent for pressure-sensitive recording paper consisting of 20% by weight or less of isopropyl biphenyl. 2. A dye solvent for pressure-sensitive recording paper comprising 60 to 75% by weight of p-isopropylbiphenyl and 25 to 40% by weight of diisopropylbiphenyl.
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62036686A JPS63203376A (en) | 1987-02-19 | 1987-02-19 | Dye solvent for pressure-sensitive recording paper and pressure-sensitive recording paper using said solvent |
| CH1764/87A CH671369A5 (en) | 1987-02-19 | 1987-05-07 | |
| GB8710770A GB2201697B (en) | 1987-02-19 | 1987-05-07 | Solvent for chromogenic dye-precursor material and pressure-sensitive recording system prepared using the solvent |
| DE19873715649 DE3715649A1 (en) | 1987-02-19 | 1987-05-11 | SOLVENTS FOR THE CHROMOGENEOUS DYE PRECURSOR MATERIAL OF A PRESSURE-SENSITIVE RECORDING PAPER AND PRINT-SENSITIVE RECORDING PAPER, MADE BY USING THE SOLVENT |
| ES8701422A ES2004286A6 (en) | 1987-02-19 | 1987-05-12 | Solvent for chromogenic dye-precursor material and pressure-sensitive recording system prepared using the solvent |
| IT20503/87A IT1204604B (en) | 1987-02-19 | 1987-05-13 | SOLVENT FOR CHROMOGEN MATERIAL PRECURSOR OF DYE FOR PRESSURE SENSITIVE RECORDING SHEET AND PRESSURE SENSITIVE RECORDING PAPER SHEET PREPARED USING SOLVENT |
| FR878706725A FR2611211B1 (en) | 1987-02-19 | 1987-05-13 | SOLVENT FOR CHROMOGENEOUS DYE PRECURSOR FOR SELF-COPYING SHEET AND SELF-COPYING SHEET PREPARED USING THE SOLVENT |
| CA000537162A CA1268629A (en) | 1987-02-19 | 1987-05-14 | Solvent for chromogenic dye-precursor material for pressure-sensitive recording paper sheet and pressure-sensitive recording paper sheet prepared by using the solvent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62036686A JPS63203376A (en) | 1987-02-19 | 1987-02-19 | Dye solvent for pressure-sensitive recording paper and pressure-sensitive recording paper using said solvent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63203376A JPS63203376A (en) | 1988-08-23 |
| JPH0441912B2 true JPH0441912B2 (en) | 1992-07-09 |
Family
ID=12476714
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62036686A Granted JPS63203376A (en) | 1987-02-19 | 1987-02-19 | Dye solvent for pressure-sensitive recording paper and pressure-sensitive recording paper using said solvent |
Country Status (8)
| Country | Link |
|---|---|
| JP (1) | JPS63203376A (en) |
| CA (1) | CA1268629A (en) |
| CH (1) | CH671369A5 (en) |
| DE (1) | DE3715649A1 (en) |
| ES (1) | ES2004286A6 (en) |
| FR (1) | FR2611211B1 (en) |
| GB (1) | GB2201697B (en) |
| IT (1) | IT1204604B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4902422A (en) * | 1988-12-06 | 1990-02-20 | Board Regents The University Of Texas System | Defect-free ultrahigh flux asymmetric membranes |
| JPH0741738B2 (en) * | 1989-03-27 | 1995-05-10 | 日本製紙株式会社 | Coloring material |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4921608B1 (en) * | 1970-08-24 | 1974-06-03 | ||
| US3627581A (en) * | 1970-10-19 | 1971-12-14 | Ncr Co | Pressure-sensitive record material |
| FR2226283A1 (en) * | 1973-04-23 | 1974-11-15 | Champion Paper Co Ltd | |
| DE2537982A1 (en) * | 1974-08-26 | 1976-03-11 | Champion Paper Co Ltd | PRESSURE SENSITIVE RECORDING MATERIAL USING ALKYLNAPHTHALINE SOLVENTS FOR DYE PRECURSORS |
| CH645306A5 (en) * | 1980-04-16 | 1984-09-28 | Ciba Geigy Ag | METHOD FOR PRODUCING CONCENTRATED SOLUTIONS OF COLOR IMAGES. |
| JPS57116686A (en) * | 1981-01-13 | 1982-07-20 | Kureha Chem Ind Co Ltd | Pressure-sensitive recording paper |
| GB2106529B (en) * | 1981-08-05 | 1985-06-12 | Monsanto Co | Solvent systems containing a high proportion of diluent for pressure-sensitive copying systems |
| JPS62257879A (en) * | 1986-05-02 | 1987-11-10 | Kureha Chem Ind Co Ltd | Dye solvent for pressure-sensitive recording paper and pressure-sensitive recording paper using said solvent |
| JPS62257880A (en) * | 1986-05-02 | 1987-11-10 | Kureha Chem Ind Co Ltd | Dye solvent for pressure-sensitive recording paper and pressure sensitive recording paper using said solvent |
-
1987
- 1987-02-19 JP JP62036686A patent/JPS63203376A/en active Granted
- 1987-05-07 CH CH1764/87A patent/CH671369A5/de not_active IP Right Cessation
- 1987-05-07 GB GB8710770A patent/GB2201697B/en not_active Expired - Fee Related
- 1987-05-11 DE DE19873715649 patent/DE3715649A1/en active Granted
- 1987-05-12 ES ES8701422A patent/ES2004286A6/en not_active Expired
- 1987-05-13 IT IT20503/87A patent/IT1204604B/en active
- 1987-05-13 FR FR878706725A patent/FR2611211B1/en not_active Expired - Fee Related
- 1987-05-14 CA CA000537162A patent/CA1268629A/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| GB8710770D0 (en) | 1987-06-10 |
| FR2611211B1 (en) | 1992-03-13 |
| GB2201697A (en) | 1988-09-07 |
| IT1204604B (en) | 1989-03-10 |
| ES2004286A6 (en) | 1988-12-16 |
| DE3715649A1 (en) | 1988-09-01 |
| IT8720503A0 (en) | 1987-05-13 |
| DE3715649C2 (en) | 1989-06-08 |
| CH671369A5 (en) | 1989-08-31 |
| GB2201697B (en) | 1991-04-24 |
| FR2611211A1 (en) | 1988-08-26 |
| CA1268629A (en) | 1990-05-08 |
| JPS63203376A (en) | 1988-08-23 |
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