CN116529021A

CN116529021A - Soldering flux and soldering paste

Info

Publication number: CN116529021A
Application number: CN202180076792.9A
Authority: CN
Inventors: 井上剑太; 宫城奈菜子; 永井智子; 高木和顺; 高木晶子
Original assignee: Senju Metal Industry Co Ltd
Current assignee: Senju Metal Industry Co Ltd
Priority date: 2020-11-18
Filing date: 2021-11-17
Publication date: 2023-08-01
Anticipated expiration: 2041-11-17
Also published as: CN116529021B

Abstract

The invention adopts soldering flux containing rosin, solvent, thixotropic agent and activator. The thixotropic agent comprises a compound represented by the general formula (1) and a polyamide, wherein the polyamide is a condensate of an amine and at least one selected from aliphatic carboxylic acids and hydroxyl-containing aliphatic carboxylic acids, and the endothermic peak temperature is 120-200 ℃. In the general formula, R ¹¹ Represents a hydrocarbon group having 11 to 30 carbon atoms. R is R ^0a Represents a hydrocarbon group having 12 to 31 carbon atoms or a hydrogen atom. R is R ^0b An n-valent hydrocarbon group having 4 to 12 carbon atoms. R is R ²¹ An alkylene group having 2 to 6 carbon atoms. R is R ^0c Represents an alkylene group having 2 to 6 carbon atoms or a single bond.n is 1 or 2. When n is 1, m is an integer of 1 to 3. When n is 2, m is 1.

Description

Soldering flux and soldering paste

Technical Field

The present invention relates to a flux and a solder paste using the same. The present application claims priority based on japanese patent application No. 2020-192036 at month 18 of 2020 and japanese patent application No. 2021-090226 at month 28 of 2021, the contents of which are incorporated herein by reference.

Background

The flux used for soldering has an effect of chemically removing a metal surface of a joining object to be soldered and a metal oxide present in solder, and enabling a metal element to move at the boundary between the two. Therefore, by performing soldering using a flux, an intermetallic compound is formed therebetween, thereby obtaining a firm joint. Such a flux generally contains a resin component, a solvent, an active agent, a thixotropic agent, and the like.

Solder paste is a composite material obtained by mixing powder of a solder alloy with flux. In soldering using a solder paste, first, after the solder paste is printed on a substrate, a component is mounted, and the substrate on which the component is mounted is heated by a heating furnace called a reflow furnace.

In the reflow oven, after preheating, main heating for melting the solder alloy powder is performed. Solder paste printed on a substrate sometimes softens when preheated, creating a heating collapse. The heat collapse causes poor mounting of solder balls, solder bridges, and the like.

In order to suppress the heat collapse at a preheating temperature of 150 ℃ to 160 ℃, for example, a flux containing a hydride of an alcohol-modified dicyclopentadiene resin has been proposed (see patent document 1).

Prior art documents

Patent literature

Patent document 1: japanese patent laid-open publication No. 2009-154170

Disclosure of Invention

Problems to be solved by the invention

In the case where the area of the substrate is large during soldering, it is required to further increase the preheating temperature in order to suppress the temperature variation in the substrate. However, for example, when the preheating temperature is 180 ℃ to 190 ℃, the flux described in patent document 1 cannot sufficiently suppress the heat collapse.

Accordingly, an object of the present invention is to provide a flux and a solder paste which can sufficiently suppress heat collapse during reflow soldering.

Means for solving the problems

In order to solve the above problems, the present invention adopts the following configuration.

That is, a first aspect of the present invention is a flux comprising rosin, a solvent, a thixotropic agent, and an active agent, wherein the thixotropic agent comprises a compound represented by the following general formula (1) and a polyamide which is a condensate of an amine and at least one selected from aliphatic carboxylic acids and hydroxyl-containing aliphatic carboxylic acids, and has an endothermic peak temperature of 120 ℃ to 200 ℃ as measured by differential scanning calorimeter.

[ chemical formula 1]

[ formula, R ¹¹ Represents a hydrocarbon group having 11 to 30 carbon atoms which may have a substituent. R is R ^0a Represents a hydrocarbon group having 12 to 31 carbon atoms or a hydrogen atom which may have a substituent. R is R ^0b Represents an n-valent hydrocarbon group having 4 to 12 carbon atoms which may have a substituent. R is R ²¹ An alkylene group having 2 to 6 carbon atoms. R is R ^0c Represents an alkylene group having 2 to 6 carbon atoms or a single bond. n is 1 or 2. When n is 1, m is an integer of 1 to 3. When n is 2, m is 1.]

In the flux of the first aspect, the polyamide is preferably an aliphatic carboxylic acid, a condensate of a hydroxyl group-containing aliphatic carboxylic acid and an amine.

In the flux according to the first aspect, the aliphatic carboxylic acid preferably contains a dicarboxylic acid.

In the flux according to the first aspect, the content of the compound represented by the general formula (1) is preferably 1% by mass or more and 10% by mass or less relative to the total mass of the flux.

In the flux according to the first aspect, the compound represented by the general formula (1) is preferably a compound represented by the following general formula (3).

[ chemical formula 2]

[ formula, R ¹¹ And R is ¹¹ ' each independently represents a hydrocarbon group having 11 to 30 carbon atoms which may have a substituent. R is R ^0a And R is ^0a ' each independently represents a hydrocarbon group having 12 to 31 carbon atoms or a hydrogen atom which may have a substituent. R is R ^0b2 Represents a hydrocarbon group having 4 to 12 carbon atoms which may have a substituent. R is R ²¹ And R is ²¹ ' each independently represents an alkylene group having 2 to 6 carbon atoms. R is R ^0c And R is ^0c ' each independently represents an alkylene group having 2 to 6 carbon atoms or a single bond.]

In the flux according to the first aspect, the compound represented by the general formula (3) is preferably N, N '-bis (2-stearamidoethyl) -sebacamide or N, N' -bis (2-stearamidoethyl) -nonyldiamide.

In the flux of the first aspect, the rosin content is preferably 30 mass% or more and 50 mass% or less with respect to the total mass of the flux.

A second aspect of the present invention is a solder paste containing a solder alloy powder and the flux described in the first aspect.

Effects of the invention

According to the present invention, it is possible to provide a flux and a solder paste which can sufficiently suppress heat collapse during reflow soldering.

Drawings

Fig. 1 is a graph showing a DSC curve of polyamide contained in the flux according to an embodiment of the present invention.

FIG. 2 is a graph showing a DSC curve of the polyamide of production example 1.

FIG. 3 is a graph showing a DSC curve of the polyamide of production example 2.

FIG. 4 is a graph showing the relationship between the heat absorption amount ratio of the polyamide in production example 1 and the temperature.

FIG. 5 is a graph showing the relationship between the heat absorption amount ratio of the polyamide in production example 2 and the temperature.

FIG. 6 is a partially enlarged view of FIG. 4, showing the relationship between the heat absorption amount ratio and the temperature of the polyamide in preparation example 1.

FIG. 7 is a partially enlarged view of FIG. 5 showing the relationship between the heat absorption amount ratio and the temperature of the polyamide in preparation example 2.

Detailed Description

(soldering flux)

The soldering flux of the present embodiment contains rosin, a solvent, a thixotropic agent, and an active agent.

< rosin >)

Examples of the rosin include: raw rosin such as gum rosin, wood rosin, and tall oil rosin, and derivatives obtained from the raw rosin.

Examples of the derivative include: purified rosin, hydrogenated rosin, disproportionated rosin, polymerized rosin, acid-modified hydrogenated rosin, phenol-modified rosin, and alpha, beta-unsaturated carboxylic acid-modified product (acrylated rosin, maleated rosin, fumarated rosin, etc.), as well as purified product, hydride, and disproportionated product of the polymerized rosin, and purified product, hydride, and disproportionated product of the alpha, beta-unsaturated carboxylic acid-modified product.

The rosin may be used alone or in combination of two or more.

Among the above, one or more kinds selected from the group consisting of polymerized rosin, acid-modified hydrogenated rosin and hydrogenated rosin are preferably used.

As the acid-modified hydrogenated rosin, acrylic acid-modified hydrogenated rosin is preferably used.

The content of rosin in the flux is preferably 30% by mass or more and 50% by mass or less, more preferably 35% by mass or more and 50% by mass or less, and still more preferably 40% by mass or more and 50% by mass or less, relative to the total amount (100% by mass) of the flux.

< solvent >

Examples of the solvent in the flux of the present embodiment include water, alcohol solvents, glycol ether solvents, terpineols, and the like.

Examples of the alcohol solvents include isopropanol, 1, 2-butanediol, isobornyl cyclohexanol, 2, 4-diethyl-1, 5-pentanediol, 2-dimethyl-1, 3-propanediol, 2, 5-dimethyl-2, 5-hexanediol, 2, 5-dimethyl-3-hexyne-2, 5-diol, 2, 3-dimethyl-2, 3-butanediol, 2-methylpentane-2, 4-diol, 1-tris (hydroxymethyl) propane, 2-ethyl-2-hydroxymethyl-1, 3-propanediol, 2' -oxybis (methylene) bis (2-ethyl-1, 3-propanediol), 2-bis (hydroxymethyl) -1, 3-propanediol, 1,2, 6-trihydroxyhexane, 1-ethynyl-1-cyclohexanol, 1, 4-cyclohexanediol, 1, 4-cyclohexanedimethanol, 2,4,7, 9-tetramethyl-5-4, 7-decanediol, and the like.

Examples of the glycol ether solvents include diethylene glycol mono-2-ethylhexyl ether, ethylene glycol monophenyl ether, diethylene glycol monohexyl ether, diethylene glycol dibutyl ether, triethylene glycol monobutyl ether, triethylene methacrylate, butyl propylene triethylene glycol, triethylene glycol butyl methyl ether, and tetraethylene glycol dimethyl ether.

As the solvent, a glycol ether type solvent is preferably used, and among them, diethylene glycol monohexyl ether is preferably used.

The solvent may be used alone or in combination of two or more.

The content of the solvent in the flux is preferably 30 mass% or more and 60 mass% or less, more preferably 30 mass% or more and 45 mass% or less, with respect to the total amount (100 mass%) of the flux.

< thixotropic agent >

In the flux of the present embodiment, the thixotropic agent contains a compound represented by the general formula (1) and a specific polyamide (PA 1).

Compounds of the general formula (1)

In the flux of the present embodiment, a compound represented by the following general formula (1) is used.

[ chemical formula 3]

R ^0b The n-valent hydrocarbon group having 4 to 12 carbon atoms may have a substituent.

In the general formula (1), when n is 2, a plurality of R ¹¹ A plurality of R ²¹ A plurality of R ^0a And a plurality of R ^0c May be different from each other or the same.

The compound represented by the above general formula (1) may be a compound represented by the following general formula (2) or a compound represented by the following general formula (3).

[ Compound represented by the general formula (2) ]

In the general formula (1), n is 1 and R ^0a is-NH-C (=O) -R ¹² ，R ^0b Is R ^0b1 ，R ^0c Is R ²² 。

[ chemical formula 4]

[ formula, R ¹¹ And R is ¹² Each independently represents a hydrocarbon group having 11 to 30 carbon atoms which may have a substituent. R is R ^0b1 Represents a hydrocarbon group having 4 to 12 carbon atoms which may have a substituent. R is R ²¹ And R is ²² Each independently represents an alkylene group having 2 to 6 carbon atoms. m is an integer of 1 to 3.]

In the general formula (2), R ¹¹ 、R ¹² And R is ^0b1 Each of the two may be a saturated hydrocarbon group or an unsaturated hydrocarbon group. R is R ¹¹ 、R ¹² And R is ^0b1 Saturated hydrocarbon groups are preferred respectively.

R ¹¹ And R is ¹² Each is preferably a hydrocarbon group having 14 to 25 carbon atoms which may have a substituent, and more preferably a hydrocarbon group having 14 to 20 carbon atoms which may have a substituent.

When R is ¹¹ Or R is ¹² When having a substituent, examples of the substituent include-CONH ₂ Amino (-NH) ₂ ) Carboxyl, and the like.

R ^0b1 The hydrocarbon group having 5 to 10 carbon atoms which may have a substituent is preferable, and the hydrocarbon group having 6 to 9 carbon atoms which may have a substituent is more preferable.

When R is ^0b1 When having a substituent, the substituent may be-CONH ₂ Amino (-NH) ₂ ) Carboxyl, and the like. In them, R ^0b1 The substituents which may be present are preferably-CONH ₂ 。

R ²¹ And R is ²² Alkylene groups having 2 carbon atoms are preferable.

m is preferably 1.

The compound represented by the above general formula (2) may be used singly or in combination of two or more.

The compound represented by the above formula (2) is preferably N, N-bis (2-stearamidoethyl) -nonyldiamide or N, N-bis (2-stearamidoethyl) -sebacamide.

N, N-bis (2-stearamidoethyl) -nonyldiamide in the above formula (2), R ¹¹ And R is ¹² Respectively straight-chain alkyl with 17 carbon atoms, R ^0b1 Is- (CH) ₂ ) ₇ -CONH ₂ ，R ²¹ And R is ²² Is an alkylene group having 2 carbon atoms, and m is 1.

N, N-bis (2-stearamidoethyl) -sebacamide in the above formula (2), R ¹¹ And R is ¹² Respectively straight-chain alkyl with 17 carbon atoms, R ^0b1 Is- (CH) ₂ ) ₈ -CONH ₂ ，R ²¹ And R is ²² Is an alkylene group having 2 carbon atoms, and m is 1.

[ Compound represented by the general formula (3) ]

In the general formula (1), n is 2, m is 1, R ^0b Is R ^0b2 。

[ chemical formula 5]

In the above general formula (3), R ¹¹ And R is ¹¹ ' may be a saturated hydrocarbon group or an unsaturated hydrocarbon group, respectively. R is R ¹¹ And R is ¹¹ ' are each preferably saturated hydrocarbon groups.

R ¹¹ And R is ¹¹ ' is preferably a hydrocarbon group having 14 to 25 carbon atoms which may have a substituent, more preferably a hydrocarbon group having 14 to 20 carbon atoms which may have a substituent.

When R is ¹¹ And R is ¹¹ When the substituent is a substituent, examples of the substituent include-CONH ₂ Amino (-NH) ₂ ) Carboxyl, and the like.

R ^0b2 Can be saturated hydrocarbon radical, alsoMay be an unsaturated hydrocarbon group. R is R ^0b2 Saturated hydrocarbon groups are preferred.

R ^0b2 The hydrocarbon group having 5 to 10 carbon atoms which may have a substituent is preferable, and the hydrocarbon group having 6 to 9 carbon atoms which may have a substituent is more preferable.

When R is ^0b2 When having a substituent, the substituent may be-CONH ₂ Amino (-NH) ₂ ) Carboxyl, and the like.

R ²¹ And R is ²¹ ' is preferably an alkylene group having 2 carbon atoms, respectively.

R ^0a R is R ^0a ' may be a saturated hydrocarbon group, an unsaturated hydrocarbon group, or a hydrogen atom, respectively.

R ^0a R is R ^0a ' is preferably a saturated hydrocarbon group or a hydrogen atom, more preferably a hydrogen atom, respectively.

R ^0c R is R ^0c ' are each preferably single bonds.

R ^0c -R ^0a And R is ^0c '-R ^0a ' is preferably a single bond-a hydrogen atom.

The compound represented by the general formula (3) is preferably N, N '-bis (2-stearamidoethyl) -nonyldiamide or N, N' -bis (2-stearamidoethyl) -sebacamide.

N, N' -bis (2-stearamidoethyl) -nonyldiamide in the above formula (3), R ¹¹ And R is ¹¹ ' is straight-chain alkyl of 17 carbon atoms, R ^0a And R is ^0a ' is a hydrogen atom, R ^0b2 Is- (CH) ₂ ) ₇ -，R ^0c And R is ^0c ' is a single bond, R ²¹ And R is ²¹ ' is an alkylene group having 2 carbon atoms.

N, N' -bis (2-stearamidoethyl) -sebacamide in the above formula (3), R ¹¹ And R is ¹¹ ' is straight-chain alkyl of 17 carbon atoms, R ^0a And R is ^0a ' is a hydrogen atom, R ^0b2 Is- (CH) ₂ ) ₈ -，R ^0c And R is ^0c ' is a single bond, R ²¹ And R is ²¹ ' is an alkylene group having 2 carbon atoms.

The compound represented by the above general formula (1) may be used singly or in combination of two or more.

The compound represented by the general formula (1) is preferably a compound represented by the general formula (2) or the general formula (3), and more preferably a compound represented by the general formula (3).

The content of the compound represented by the general formula (1) in the flux is preferably 1% by mass or more and 10% by mass or less relative to the total amount (100% by mass) of the flux.

Polyamide (PA 1)

In the flux of the present embodiment, a specific polyamide (PA 1) is used. The specific polyamide (PA 1) is a condensate of an amine and at least one selected from aliphatic carboxylic acids and hydroxyl-containing aliphatic carboxylic acids.

Specific polyamides (PA 1) include "condensates of aliphatic carboxylic acids with amines", "condensates of hydroxy-containing aliphatic carboxylic acids with amines" and "condensates of hydroxy-containing aliphatic carboxylic acids, aliphatic carboxylic acids with amines".

The temperature of the endothermic peak of the specific polyamide (PA 1) measured by differential scanning calorimeter is 120 ℃ to 200 ℃.

The aliphatic carboxylic acid from which the specific polyamide (PA 1) is derived may be used singly or in combination of two or more.

Examples of the aliphatic carboxylic acid include monocarboxylic acids, dicarboxylic acids, and tricarboxylic acids. The aliphatic carboxylic acid is preferably a monocarboxylic acid or a dicarboxylic acid, more preferably a dicarboxylic acid.

The hydrocarbon group of the aliphatic carboxylic acid may be any of linear, branched or cyclic. The hydrocarbon group is preferably linear or branched, and more preferably linear.

The hydrocarbon group may be a saturated hydrocarbon group or an unsaturated hydrocarbon group. The hydrocarbyl group is preferably a saturated hydrocarbyl group.

The number of carbon atoms of the aliphatic monocarboxylic acid is preferably 12 to 22, more preferably 14 to 22, and still more preferably 16 to 22.

Examples of the aliphatic monocarboxylic acid include lauric acid, myristic acid, pentadecanoic acid, palmitic acid, margaric acid, stearic acid, nonadecanoic acid, arachic acid, and behenic acid. The aliphatic monocarboxylic acid is preferably palmitic acid or stearic acid.

The aliphatic dicarboxylic acid preferably has 2 to 20 carbon atoms, more preferably 6 to 16 carbon atoms, and still more preferably 8 to 14 carbon atoms.

Examples of the aliphatic dicarboxylic acid include adipic acid, pimelic acid, suberic acid, azelaic acid, sebacic acid, undecanedioic acid, dodecanedioic acid, tridecanedioic acid, tetradecanedioic acid, pentadecanedioic acid, and the like. The aliphatic dicarboxylic acid is preferably suberic acid, azelaic acid, sebacic acid, undecanedioic acid or dodecanedioic acid, more preferably sebacic acid or dodecanedioic acid.

The aliphatic carboxylic acid may contain one or more selected from sebacic acid and dodecanedioic acid, and one or more selected from palmitic acid and stearic acid.

The hydroxyl group-containing aliphatic carboxylic acid from which the specific polyamide (PA 1) is derived may be used singly or in combination of two or more.

The hydrocarbon group of the hydroxyl group-containing aliphatic carboxylic acid may be any of linear, branched or cyclic. The hydrocarbon group is preferably linear or branched, and more preferably linear.

The number of carbon atoms of the hydroxyl group-containing aliphatic carboxylic acid is preferably 10 to 25, more preferably 15 to 21.

Examples of the above-mentioned hydroxyl-containing aliphatic carboxylic acid include hydroxypentadecanoic acid, hydroxyhexadecanoic acid, hydroxyheptadecanoic acid, hydroxyoctadecanoic acid (hydroxystearic acid), hydroxyeicosanoic acid, and hydroxydi-undecanoic acid. The hydroxyl-containing aliphatic carboxylic acid is preferably hydroxystearic acid, more preferably 12-hydroxystearic acid.

The amine from which the specific polyamide (PA 1) is derived may be used singly or in combination of two or more.

Examples of the amine include aliphatic amines and aromatic amines. The amine is preferably an aliphatic amine.

Examples of the amine include monoamine, diamine, triamine, and tetramine. The amine is preferably a diamine.

The hydrocarbon group of the aliphatic amine may be any of linear, branched or cyclic. The hydrocarbon group is preferably linear or branched, and more preferably linear. The aliphatic amine preferably has 3 to 10 carbon atoms, more preferably 4 to 8 carbon atoms.

Examples of the amine include ethylenediamine, 1, 3-propylenediamine, 1, 4-butylenediamine, hexamethylenediamine, m-xylylenediamine, toluenediamine, p-xylylenediamine, phenylenediamine, isophoronediamine, 1, 10-decylenediamine, 1, 12-dodecylenediamine, 4-diaminodicyclohexylmethane, 4-diaminodiphenylmethane, butane-1, 4-tetramine, pyrimidine-2, 4,5, 6-tetramine, and the like. The amine is preferably hexamethylenediamine.

The temperature of the endothermic peak of the polyamide was measured by DSC (Differential Scanning Calorimetry, differential scanning calorimeter).

As a specific method for measuring the endothermic peak, the temperature rise rate was set at 20℃per minute, and about 10mg of polyamide was measured under a nitrogen atmosphere by raising the temperature from 25℃to 350 ℃. As the measuring instrument, DSC7020 (hitachi high tech) can be used. In the present specification, the temperature of the endothermic peak means the temperature of the peak top.

The specific polyamide (PA 1) used in the flux of the present embodiment has 1 or 2 or more endothermic peaks in a temperature range of 120 ℃ or more and 200 ℃ or less.

When the number of endothermic peaks is 1, the temperature of the endothermic peaks is preferably 150 ℃ or more and 200 ℃ or less, more preferably 160 ℃ or more and 200 ℃ or less, still more preferably 170 ℃ or more and 200 ℃ or less, particularly preferably 180 ℃ or more and 200 ℃ or less.

When the number of endothermic peaks is 2 or more, for example, the lowest temperature endothermic peak of the polyamide (PA 1) may be in the range of 120 ℃ or more and 200 ℃ or less, the highest temperature endothermic peak may be in the range of 120 ℃ or more and 200 ℃ or less, or all the endothermic peaks may be in the range of 120 ℃ or more and 200 ℃ or less.

The temperature of the highest temperature endothermic peak is preferably 150 ℃ or more and 200 ℃ or less, more preferably 160 ℃ or more and 200 ℃ or less, still more preferably 170 ℃ or more and 200 ℃ or less, particularly preferably 180 ℃ or more and 200 ℃ or less.

The proportion of the heat absorption amount in the range of 160 ℃ to 200 ℃ is preferably 30% or more, more preferably 40% or more, and even more preferably 45% or more, relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ as measured by DSC of the polyamide (PA 1).

The upper limit of the heat absorption amount is not particularly limited as long as the effect of the present invention can be achieved, and may be, for example, 80% or less, 70% or less, or 60% or less.

The heat absorption amount is preferably 30% to 80%, more preferably 40% to 80%, and still more preferably 45% to 80%. Alternatively, the heat absorption amount is preferably 30% or more and 70% or less, more preferably 40% or more and 70% or less, and still more preferably 45% or more and 70% or less.

The heat absorption amount in the range of 160 ℃ to 200 ℃ is not less than the lower limit value as measured by DSC of polyamide (PA 1), and heat collapse at the time of reflow soldering can be sufficiently suppressed. In particular, even when the temperature of the preheating is increased, for example, 190 ℃ or higher, and further 200 ℃ or higher, the heating collapse can be suppressed.

In the present specification, the heat absorption amount of polyamide can be calculated from the peak area of the DSC curve of polyamide.

The proportion of the heat absorption amount in the range of 50 ℃ to 150 ℃ is preferably 80% or less, more preferably 60% or less, and even more preferably 50% or less, relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ as measured by DSC of the polyamide (PA 1).

The lower limit of the heat absorption amount ratio is not particularly limited as long as the effect of the present invention can be achieved, and may be, for example, 10% or more, 20% or more, or 30% or more.

The heat absorption amount is preferably 10% to 80%, more preferably 10% to 60%, still more preferably 10% to 50%. Alternatively, the heat absorption amount is preferably 20% or more and 80% or less, more preferably 20% or more and 60% or less, and still more preferably 20% or more and 50% or less.

The proportion of the heat absorption amount in the range of 50 ℃ to 180 ℃ is preferably 95% or less, more preferably 90% or less, and even more preferably 85% or less, relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ as measured by DSC of the polyamide (PA 1).

The lower limit of the heat absorption amount is not particularly limited as long as the effect of the present invention can be achieved, and may be, for example, 40% or more, 50% or more, or 60% or more.

The heat absorption amount is preferably 40% to 95%, more preferably 40% to 90%, and even more preferably 40% to 85%. Alternatively, the heat absorption amount is preferably 50% or more and 95% or less, more preferably 50% or more and 90% or less, and still more preferably 50% or more and 85% or less.

The specific polyamide (PA 1) contained in the flux of the present embodiment is preferably a condensate of an aliphatic carboxylic acid, a hydroxyl group-containing monocarboxylic acid, and an amine from the viewpoint of further improving the heat collapse suppressing ability.

The specific polyamide (PA 1) contained in the flux of the present embodiment is more preferably a condensate of a dicarboxylic acid, a hydroxyl group-containing monocarboxylic acid, and a diamine. The specific polyamide (PA 1) contained in the flux of the present embodiment is more preferably a condensate of an aliphatic dicarboxylic acid having 8 to 14 carbon atoms, a hydroxyl group-containing aliphatic monocarboxylic acid having 15 to 21 carbon atoms, and an aliphatic diamine having 4 to 8 carbon atoms.

Among them, polyamide (PA 1) is particularly preferably a condensate of 12-hydroxystearic acid and hexamethylenediamine, which is one or more selected from sebacic acid and dodecanedioic acid.

The polyamide (PA 1) may be a condensate of 12-hydroxystearic acid and hexamethylenediamine, and at least one selected from sebacic acid and dodecanedioic acid, and at least one selected from palmitic acid and stearic acid.

When the polyamide (PA 1) is a condensate of an aliphatic dicarboxylic acid, a hydroxyl group-containing aliphatic monocarboxylic acid and an aliphatic diamine, the molar ratio of these raw materials preferably satisfies the following relational expression.

Here, the aliphatic dicarboxylic acid used as the raw material of the polyamide (PA 1) is X moles, the hydroxyl group-containing aliphatic monocarboxylic acid is Y moles, and the aliphatic diamine is Z moles.

Preferably, the total number of moles of amino groups of the compound contained in the raw material is equal to the total number of moles of carboxyl groups, or the total number of moles of amino groups of the compound contained in the raw material is smaller than the total number of moles of carboxyl groups. Specifically, it is preferable to satisfy 2Z.ltoreq.2X+Y.

The relation of the molar ratio between the raw materials is preferably 0.2 Y.ltoreq.X.ltoreq.2Y, more preferably 0.4 Y.ltoreq.X.ltoreq.1.5Y.

The relation of the molar ratio between the raw materials is preferably 0.5 Y.ltoreq.Z.ltoreq.2Y, more preferably 0.8 Y.ltoreq.Z.ltoreq.1.8Y.

The content of polyamide (PA 1) in the flux is preferably 1% by mass or more and 15% by mass or less, more preferably 2% by mass or more and 10% by mass or less, and still more preferably 3% by mass or more and 6% by mass or less, relative to the total amount (100% by mass) of the flux.

The proportion of the compound represented by the general formula (1) is preferably 10% by mass or more and 90% by mass or less, more preferably 15% by mass or more and 75% by mass or less, based on the total mass (100% by mass) of the compound represented by the general formula (1) and the specific polyamide (PA 1).

Other thixotropic agents

The thixotropic agent may contain other thixotropic agents in addition to the compound represented by the above general formula (1) and the polyamide (PA 1).

Examples of the other thixotropic agent include amide-based thixotropic agents, wax-based thixotropic agents, sorbitol-based thixotropic agents, and the like other than the above.

The other thixotropic agent may be used alone or in combination of two or more.

Examples of the amide thixotropic agent other than the above include monoamides, bisamides, and other polyamides.

Examples of the monoamide include lauric acid amide, palmitic acid amide, stearic acid amide, behenic acid amide, hydroxystearic acid amide, saturated fatty acid amide, oleic acid amide, erucic acid amide, unsaturated fatty acid amide, p-toluamide, aromatic amide, hexamethylenehydroxystearic acid amide, substituted amide, methylol stearic acid amide, methylol amide, fatty acid ester amide, and the like.

Examples of the bisamide include methylene bisstearamide, ethylene bislauramide, ethylene bishydroxy fatty acid (C6 to C24 fatty acid) amide, ethylene bisstearamide, ethylene bishydroxy stearamide, saturated fatty acid bisamide, methylene bisoleamide, unsaturated fatty acid bisamide, m-xylylene bisstearamide, and aromatic bisamide.

Examples of the other polyamide include saturated fatty acid polyamide, unsaturated fatty acid polyamide, aromatic polyamide, 1,2, 3-propane tricarboxylic acid tris (2-methylcyclohexylamide), cyclic amide oligomer, and acyclic amide oligomer.

Examples of the cyclic amide oligomer include an amide oligomer obtained by polycondensation of a dicarboxylic acid and a diamine into a ring, an amide oligomer obtained by polycondensation of a tricarboxylic acid and a diamine into a ring, an amide oligomer obtained by polycondensation of a dicarboxylic acid and a triamine into a ring, an amide oligomer obtained by polycondensation of a tricarboxylic acid and a triamine into a ring, an amide oligomer obtained by polycondensation of a dicarboxylic acid and a tricarboxylic acid with a diamine into a ring, an amide oligomer obtained by polycondensation of a dicarboxylic acid and a tricarboxylic acid with a triamine into a ring, an amide oligomer obtained by polycondensation of a dicarboxylic acid and a diamine and a triamine into a ring, an amide oligomer obtained by polycondensation of a tricarboxylic acid and a tricarboxylic acid with a diamine and a triamine into a ring.

Examples of the acyclic amide oligomer include an amide oligomer obtained by polycondensation of a monocarboxylic acid and a diamine and/or a triamine into an acyclic state, and an amide oligomer obtained by polycondensation of a dicarboxylic acid and/or a tricarboxylic acid and a monoamine into an acyclic state. In the case of an amide oligomer containing a monocarboxylic acid or a monoamine, the monocarboxylic acid or the monoamine functions as a terminal molecule (terminal molecules) and becomes an acyclic amide oligomer having a reduced molecular weight. In the case of an amide compound obtained by polycondensation of a dicarboxylic acid and/or a tricarboxylic acid with a diamine and/or a triamine to form an acyclic amide compound, the acyclic amide oligomer is an acyclic high molecular weight amide polymer. The acyclic amide oligomer further includes an amide oligomer obtained by condensing a monocarboxylic acid and a monoamine into an acyclic form.

The total content of the amide-based thixotropic agent in the flux is preferably 3 mass% or more and 30 mass% or less, more preferably 4 mass% or more and 20 mass% or less, and still more preferably 5.5 mass% or more and 14.5 mass% or less, with respect to the total amount (100 mass%) of the flux.

Examples of the wax-based thixotropic agent include ester compounds, specifically hydrogenated castor oil and the like.

The content of the wax-based thixotropic agent in the flux is preferably 0 mass% or more and 10 mass% or less, more preferably 0 mass% or more and 5 mass% or less, and still more preferably 0 mass% or more and 3 mass% or less, with respect to the total amount (100 mass%) of the flux.

Examples of sorbitol thixotropic agents include dibenzylidene-D-sorbitol, di (4-methylbenzylidene) -D-sorbitol, (D-) sorbitol, monobenzyl (-D-) sorbitol, and mono (4-methylbenzylidene) - (D-) sorbitol.

The content of the sorbitol thixotropic agent in the flux is preferably 0 mass% or more and 5.0 mass% or less, more preferably 0 mass% or more and 3.5 mass% or less, with respect to the total amount (100 mass%) of the flux.

The total content of the thixotropic agent in the flux is preferably 2 mass% or more and 30 mass% or less, more preferably 4 mass% or more and 20 mass% or less, and still more preferably 5 mass% or more and 15 mass% or less, with respect to the total amount (100 mass%) of the flux.

The content of the other thixotropic agent in the flux is preferably 0 mass% or more and 10 mass% or less, more preferably 0 mass% or more and 5 mass% or less, with respect to the total amount (100 mass%) of the flux.

The proportion of the other thixotropic agent in the flux is preferably 0 mass% or more and 50 mass% or less, more preferably 0 mass% or more and 30 mass% or less, and still more preferably 0 mass% or more and 20 mass% or less, relative to the total mass (100 mass%) of the thixotropic agent.

< active agent >

Examples of the active agent include organic acids, halogen-based active agents, and amines.

Organic acid:

examples of the organic acid include glutaric acid, adipic acid, azelaic acid, eicosanedioic acid, citric acid, glycolic acid, succinic acid, salicylic acid, diglycolic acid, dipicolinic acid, dibutylanilino diglycolic acid, suberic acid, sebacic acid, thioglycolic acid, dimercaptoacetic acid, terephthalic acid, dodecanedioic acid, p-hydroxyphenylacetic acid, picolinic acid, phenylsuccinic acid, phthalic acid, fumaric acid, maleic acid, malonic acid, lauric acid, benzoic acid, tartaric acid, tris (2-carboxyethyl) isocyanurate, glycine, 1, 3-cyclohexanedicarboxylic acid, 2-bis (hydroxymethyl) propionic acid, 2-bis (hydroxymethyl) butyric acid, 2, 3-dihydroxybenzoic acid, 2, 4-diethylglutaric acid, 2-quinolinecarboxylic acid, 3-hydroxybenzoic acid, propionic acid, malic acid, p-anisic acid, stearic acid, 12-hydroxystearic acid, oleic acid, linoleic acid, linolenic acid, palmitic acid, pimelic acid, dimer acid, trimer acid, hydrogenated dimer acid as a hydrogenated dimer of dimer acid, and trimer acid as a hydrogenated product of dimer acid.

The organic acid may be used alone or in combination of two or more.

The organic acid is preferably a dicarboxylic acid.

The dicarboxylic acid is preferably one or more selected from glutaric acid, adipic acid, pimelic acid, suberic acid, azelaic acid and sebacic acid, more preferably one or more selected from glutaric acid, adipic acid and azelaic acid.

The total content of the organic acid in the flux is preferably 3 mass% or more and 10 mass% or less, more preferably 5 mass% or more and 8 mass% or less, with respect to the total amount (100 mass%) of the flux.

Halogen-based active agents:

examples of the halogen-based active agent include halogenated aliphatic compounds and amine halogen acid salts.

The halogen-based active agent may be used alone or in combination of two or more.

Examples of the halogenated aliphatic compound include 1-bromo-2-propanol, 3-bromo-1, 2-propanediol, 1-bromo-2-butanol, 1, 3-dibromo-2-propanol, 2, 3-dibromo-1-propanol, 1, 4-dibromo-2-butanol, 2, 3-dibromo-1, 4-butanediol, and trans-2, 3-dibromo-2-butene-1, 4-diol.

The amine hydrohalate is a compound obtained by reacting an amine with a hydrogen halide, and examples of the amine include ethylamine, diethylamine, triethylamine, ethylenediamine, 1, 3-diphenylguanidine, 1, 3-di-o-tolylguanidine, and 1-o-tolylguanidine, and examples of the hydrogen halide include hydrogen chloride, bromine, and iodine hydrides.

The flux of the present embodiment preferably contains a halogen-based active agent.

The flux of the present embodiment preferably contains a halogenated aliphatic compound.

The halogenated aliphatic compound is preferably trans-2, 3-dibromo-2-butene-1, 4-diol.

The total content of the halogen-based active agent in the flux is preferably 0 mass% or more and 5 mass% or less with respect to the total amount (100 mass%) of the flux.

Amine:

examples of the amine include: ethylamine, triethylamine, ethylenediamine, triethylenetetramine, 2-methylimidazole, 2-undecylimidazole, 2-heptadecylimidazole, 1, 2-dimethylimidazole, 2-ethyl-4-methylimidazole, 2-phenylimidazole, 2-phenyl-4-methylimidazole, 1-benzyl-2-phenylimidazole, 1-cyanoethyl-2-methylimidazole, 1-cyanoethyl-2-undecylimidazole, 1-cyanoethyl-2-ethyl4-methylimidazole, 1-cyanoethyl-2-phenylimidazole, 1-cyanoethyl-2-undecylimidazole trimellitate, 1-cyanoethyl-2-phenylimidazole trimellitate, 2, 4-diamino-6- [2 "-methylimidazole- (1 ') ] -ethyl s triazine, 2, 4-diamino-6- [2' -undecylimidazole- (1 ') ] -ethyl s triazine, 2, 4-diamino-6- [2' -ethyl-4 ' -methylimidazole- (1 ') ] -ethyl s triazine, 2, 4-diamino-6- [2' -methyl-4 ' -imidazol- (1 ') ] -ethyl s triazine, 2, 4-diamino-6- [2' -methyl-imidazol-trimellitate, 1' -methyl-2 ' -phenyl-imidazolyl-trimellitate, 2' -hydroxy-phenyl-imidazole, 3-d-hydroxy-methyl-5-isocyanuric acid, and isocyanuric acid adduct, 3-hydroxy-methyl-5-phenyl-imidazole, and 3-d, 2-phenyl-4-methyl-5-hydroxymethyl imidazole, 2, 3-dihydro-1H-pyrrolo [1,2-a ] benzimidazole, 1-dodecyl-2-methyl-3-benzyl imidazole chloride, 2-methylimidazoline, 2-phenylimidazoline, 2, 4-diamino-6-vinyl-s-triazine, 2, 4-diamino-4, 6-vinyl-s-triazine isocyanuric acid adduct, 2, 4-diamino-6-methacryloyloxyethyl-s-triazine, epoxy-imidazole adduct, 2-methylbenzimidazole, 2-octylbenzimidazole, 2-pentylbenzoimidazole, 2- (1-ethylpentyl) benzimidazole, 2-nonylbenzimidazole, 2- (4-thiazolyl) benzimidazole, 2- (2 ' -hydroxy-5 ' -methylphenyl) benzotriazole, 2- (2 ' -hydroxy-3 ',5' -di-tert-pentylphenyl) benzotriazole, 2- (2 ' -hydroxy-5 ' -tert-octylphenyl) benzotriazole, 2' -bis [ 2- (2-ethylphenyl) -benzotriazole, 2-bis [ 2-hydroxy-5 ' -methylphenyl ] benzotriazole, 2- (2-hydroxy-3 ',5' -di-tert-pentylpheno) benzotriazole, 2-4-octylphenol, 6- (2-benzotriazolyl) -4-tert-octyl-6 '-tert-butyl-4' -methyl-2, 2 '-methylenebisphenol, 1,2, 3-benzotriazole, 1- [ N, N-bis (2-ethylhexyl) aminomethyl ] benzotriazole, carboxybenzotriazole, 1- [ N, N-bis (2-ethylhexyl) aminomethyl ] methylbenzotriazole, 2' - [ [ (methyl-1H-benzotriazol-1-yl) methyl ] imino ] bisethanol, 1- (1 ',2' -dicarboxyethyl) benzotriazole, 1- (2, 3-dicarboxypropyl) benzotriazole, 1- [ (2-ethylhexyl amino) methyl ] benzotriazole, 2, 6-bis [ (1H-benzotriazol-1-yl ] methyl ] -4-methylphenol, 5-methylbenzotriazole, 5-phenyltetrazole, and the like.

The amine may be used alone or in combination of two or more.

The amine is preferably at least one selected from 2-phenylimidazole and 2-phenyl-4-methylimidazole.

The content of amine in the flux is preferably more than 0% by mass and 20% by mass or less, more preferably more than 0% by mass and 10% by mass or less, still more preferably more than 0% by mass and 3% by mass or less, and particularly preferably more than 0% by mass and 1% by mass or less, relative to the total amount (100% by mass) of the flux.

< other Components >)

The flux of the present embodiment may contain other components in addition to rosin, solvent, thixotropic agent, and active agent.

Examples of the other component include a surfactant, a silane coupling agent, and a colorant.

Examples of the surfactant include nonionic surfactants and weak cationic surfactants.

Examples of the nonionic surfactant include polyethylene glycol, polyethylene glycol-polypropylene glycol copolymer, aliphatic alcohol polyoxyethylene adduct, aromatic alcohol polyoxyethylene adduct, and polyhydric alcohol polyoxyethylene adduct.

Examples of the weak cationic surfactant include terminal diamine polyethylene glycol, terminal diamine polyethylene glycol-polypropylene glycol copolymer, aliphatic amine polyoxyethylene adduct, aromatic amine polyoxyethylene adduct, and polyamine polyoxyethylene adduct.

Examples of the surfactant other than the above-mentioned surfactant include polyoxyalkylene acetylene glycols, polyoxyalkylene glycerol ethers, polyoxyalkylene alkyl ethers, polyoxyalkylene esters, polyoxyalkylene alkylamines, polyoxyalkylene alkylamides, and the like.

In addition, in the flux of the present embodiment, an antioxidant may be used for the purpose of suppressing oxidation of the solder alloy powder. As the antioxidant, a hindered phenol-based antioxidant such as 2,2' -methylenebis [6- [ 1-methylcyclohexyl ] -p-cresol ] can be used.

Additives such as a matting agent and a defoaming agent may be further added to the flux of the present embodiment.

The flux of the present embodiment described above can sufficiently suppress heat collapse at the time of reflow soldering by using the specific amide compound represented by the general formula (1) and the specific polyamide in combination as a thixotropic agent. In particular, even in the case where the temperature of the preheating is increased, for example, 190 ℃ or higher, further 200 ℃ or higher, by applying this combination, the heating collapse can be suppressed.

(solder paste)

The solder paste of the present embodiment contains the solder alloy powder and the flux described above.

The solder alloy powder may be composed of a powder of a solder of Sn alone, or of Sn-Ag, sn-Cu, sn-Ag-Cu, sn-Bi a powder of a solder alloy such as sn—in or a powder of a solder alloy such as Sb, bi, in, cu, zn, as, ag, cd, fe, ni, co, au, ge, P added to these alloys.

The solder alloy powder may be composed of a powder in which a solder alloy such as Sb, bi, in, cu, zn, as, ag, cd, fe, ni, co, au, ge, P is added to a Sn-Pb system or a Sn-Pb system.

The solder alloy powder is preferably Pb-free solder.

Content of soldering flux:

the content of the flux in the solder paste is preferably 5 to 30 mass%, more preferably 5 to 15 mass%, relative to the total mass of the solder paste.

The solder paste of the present embodiment contains the flux described above, and thus sufficiently suppresses heat collapse.

The flux of the present embodiment may be any other embodiment than the above. In this other embodiment, the flux contains rosin, a solvent, a specific thixotropic agent, and an activator.

< rosin >)

The rosin used in the flux of the other embodiment is the above-described one.

The rosin may be used alone or in combination of two or more.

The content of rosin in the flux according to another embodiment is preferably 30 mass% or more and 50 mass% or less, more preferably 30 mass% or more and 40 mass% or less, with respect to the total amount (100 mass%) of the flux.

< solvent >

The solvent used in the flux of the other embodiment includes the solvent described above.

The solvent may be used alone or in combination of two or more.

The content of the solvent in the flux according to this other embodiment is preferably 30 mass% or more and 60 mass% or less, more preferably 35 mass% or more and 55 mass% or less, with respect to the total amount (100 mass%) of the flux.

Specific thixotropic agent

The flux of this other embodiment contains polyamide (PA 2) as a specific thixotropic agent.

The polyamide (PA 2) is a condensate of an aliphatic amine having 3 to 10 carbon atoms and at least one member selected from aliphatic carboxylic acids and hydroxyl-containing aliphatic carboxylic acids.

Specifically, the polyamide (PA 2) is a material in which an amine that is a raw material of the polyamide (PA 1) is specified as an aliphatic amine having 3 to 10 carbon atoms.

The aliphatic carboxylic acid from which the polyamide (PA 2) is derived may be used singly or in combination of two or more.

The number of carbon atoms of the aliphatic dicarboxylic acid is preferably 11 to 20, more preferably 12 to 18, and still more preferably 12 to 16.

Examples of the aliphatic dicarboxylic acid include dodecanedioic acid, tridecanedioic acid, tetradecanedioic acid, pentadecanedioic acid, and the like. The aliphatic dicarboxylic acid is preferably dodecanedioic acid.

The aliphatic carboxylic acid may contain dodecanedioic acid and one or more selected from palmitic acid and stearic acid.

The hydroxyl group-containing aliphatic carboxylic acid from which the polyamide (PA 2) is derived may be used singly or in combination.

The amine derived from the polyamide (PA 2) is an aliphatic amine having 3 to 10 carbon atoms. The amine from which the polyamide (PA 2) is derived may be used singly or in combination of two or more.

Examples of the aliphatic amine include monoamines, diamines, triamines, and tetramines. The amine is preferably a diamine.

The hydrocarbon group of the aliphatic amine may be any of linear, branched or cyclic. The hydrocarbon group is preferably linear or branched, and more preferably linear. The aliphatic amine preferably has 4 to 8 carbon atoms.

Examples of the aliphatic amine include 1, 3-propanediamine, 1, 4-butanediamine, hexamethylenediamine, butane-1, 4-tetramine, and the like. The aliphatic amine is preferably hexamethylenediamine.

The polyamide (PA 2) is preferably a condensate of an aliphatic carboxylic acid, a hydroxyl group-containing monocarboxylic acid, and an aliphatic diamine having 3 to 10 carbon atoms.

The polyamide (PA 2) is more preferably a condensate of an aliphatic dicarboxylic acid having 12 to 20 carbon atoms, a hydroxyl group-containing monocarboxylic acid having 15 to 21 carbon atoms, and an aliphatic diamine having 4 to 8 carbon atoms.

Among them, polyamide (PA 2) is more preferably a condensate of dodecanedioic acid, 12-hydroxystearic acid and hexamethylenediamine.

The polyamide (PA 2) may be dodecanedioic acid, one or more selected from palmitic acid and stearic acid, or a condensate of 12-hydroxystearic acid and hexamethylenediamine.

The polyamide (PA 2) has the following characteristics.

The heat absorption amount in the range of 50 ℃ to 190 ℃ is preferably 90% or more, more preferably 92% or more, and even more preferably 94% or more, relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ by DSC measurement of polyamide (PA 2).

The proportion of the heat absorption amount is preferably a high value. The upper limit of the amount of heat absorption is not particularly limited as long as the effect of the present invention can be achieved, and may be, for example, 100%.

The heat absorption amount is preferably 90% or more and 100% or less, more preferably 92% or more and 100% or less, and still more preferably 94% or more and 100% or less.

When the ratio of the amount of heat absorption is equal to or greater than the lower limit value, the ability to suppress void generation can be easily improved.

The heat absorption amount in the range of 50 ℃ to 195 ℃ is preferably 96% or more, more preferably 98% or more, and still more preferably 99% or more relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ by DSC measurement of polyamide (PA 2).

The heat absorption amount is preferably 96% to 100%, more preferably 98% to 100%, and even more preferably 99% to 100%.

The proportion of the heat absorption amount in the range of 160 ℃ to 200 ℃ by DSC of the polyamide (PA 2) is preferably 30% or more, more preferably 40% or more, and even more preferably 45% or more with respect to the total heat absorption amount in the range of 50 ℃ to 200 ℃.

The upper limit value of the heat absorption amount ratio is not particularly limited as long as the effect of the present invention can be achieved, and may be, for example, 80% or less, 70% or less, or 60% or less.

The heat absorption amount is preferably 30% to 80%, more preferably 40% to 80%, and still more preferably 45% to 80%. Alternatively, the heat absorption amount is preferably 30% or more and 70% or less, more preferably 40% or more and 70% or less, and still more preferably 45% or more and 70% or less. The heat absorption amount ratio in the range of 160 ℃ to 200 ℃ is not less than the lower limit value by DSC measurement of polyamide (PA 2), and heat collapse during reflow soldering can be sufficiently suppressed. In particular, even when the temperature of the preheating is increased, for example, 190 ℃ or higher, and further 200 ℃ or higher, the heating collapse can be suppressed.

The proportion of the heat absorption amount in the range of 50 ℃ to 150 ℃ is preferably 80% or less, more preferably 60% or less, and even more preferably 50% or less, relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ as measured by DSC of the polyamide (PA 2).

The proportion of the heat absorption amount in the range of 50 ℃ to 180 ℃ is preferably 95% or less, more preferably 90% or less, and even more preferably 85% or less, relative to the total heat absorption amount in the range of 50 ℃ to 200 ℃ as measured by DSC of the polyamide (PA 2).

The polyamide (PA 2) has 1 or 2 or more endothermic peaks in a temperature range of 120 ℃ or more and 200 ℃ or less as measured by DSC.

When the number of endothermic peaks is 2 or more, for example, the lowest temperature endothermic peak of the polyamide (PA 2) may be in the range of 120 ℃ or more and 200 ℃ or less, the highest temperature endothermic peak may be in the range of 120 ℃ or more and 200 ℃ or less, or all the endothermic peaks may be in the range of 120 ℃ or more and 200 ℃ or less.

The polyamide (PA 2) preferably has three endothermic peaks in the DSC curve consisting of a first endothermic peak, a second endothermic peak and a third endothermic peak.

The temperature of the first endothermic peak is preferably lower than 150 ℃, more preferably from 120 ℃ to 140 ℃, still more preferably from 125 ℃ to 135 ℃, particularly preferably from 125 ℃ to 130 ℃.

The temperature of the second endothermic peak is preferably 150 ℃ or higher, more preferably 155 ℃ or higher and 175 ℃ or lower, still more preferably 160 ℃ or higher and 170 ℃ or lower, particularly preferably 162 ℃ or higher and 167 ℃ or lower.

The temperature of the third endothermic peak is preferably 150 ℃ or higher, more preferably 180 ℃ or higher and 196 ℃ or lower, still more preferably 183 ℃ or higher and 195 ℃ or lower, particularly preferably 185 ℃ or higher and 193 ℃ or lower.

When the polyamide (PA 2) is a condensate of an aliphatic dicarboxylic acid, a hydroxyl group-containing aliphatic monocarboxylic acid and an aliphatic diamine, the molar ratio of these raw materials preferably satisfies the following relational expression.

Here, the aliphatic dicarboxylic acid used as the raw material of the polyamide (PA 2) is X moles, the hydroxyl group-containing aliphatic monocarboxylic acid is Y moles, and the aliphatic diamine is Z moles.

The content of the polyamide (PA 2) is preferably 0.5 mass% or more and 20 mass% or less, more preferably 1 mass% or more and 20 mass% or less, still more preferably 2 mass% or more and 20 mass% or less, particularly preferably 5 mass% or more and 20 mass% or less, and most preferably 15 mass% or more and 20 mass% or less, relative to the total amount (100 mass%) of the flux.

< other Components >)

In addition, the flux of this other embodiment may further contain other components in addition to rosin, solvents, specific thixotropic agents, and active agents.

Examples of the other components include thixotropic agents other than polyamide (PA 2), surfactants, silane coupling agents, and colorants.

Examples of the other thixotropic agent include an amide-based thixotropic agent other than polyamide (PA 2), a wax-based thixotropic agent, and a sorbitol-based thixotropic agent.

The other thixotropic agent may be used alone or in combination of two or more.

The total content of the amide-based thixotropic agent in the flux is preferably 0.5 mass% or more and 30 mass% or less, more preferably 0.5 mass% or more and 20 mass% or less, and still more preferably 5 mass% or more and 20 mass% or less, with respect to the total amount (100 mass%) of the flux.

The content of the wax-based thixotropic agent in the flux is preferably 0 mass% or more and 10 mass% or less, more preferably 2 mass% or more and 7 mass% or less, and still more preferably 3 mass% or more and 6 mass% or less, with respect to the total amount (100 mass%) of the flux.

The content of the wax-based thixotropic agent in the flux is preferably 12 mass% or more and 100 mass% or less, more preferably 18 mass% or more and 100 mass% or less, still more preferably 33 mass% or more and 100 mass% or less, and particularly preferably 60 mass% or more and 100 mass% or less, relative to the total amount (100 mass%) of the amide-based thixotropic agent and the wax-based thixotropic agent.

In the flux of this other embodiment, the polyamide (PA 2) contained in the flux melts at 190 ℃ and 195 ℃ and the fluidity is sufficiently high, so that the occurrence of voids can be sufficiently suppressed.

In addition, in the flux according to the other embodiment, the polyamide (PA 2) contained in the flux is not partially melted at 150 ℃ and 180 ℃, and thus the heat collapse can be sufficiently suppressed. In particular, even when the temperature of the preheating is increased, for example, 190 ℃ or higher, and further 200 ℃ or higher, the heating collapse can be suppressed.

(solder paste)

Other embodiments of the solder paste contain solder alloy powder and flux from the other embodiments.

The solder alloy powder may be composed of a powder of a solder of Sn alone, or of Sn-Ag, sn-Cu, sn-Ag-Cu, sn-Bi a powder of a solder alloy such as sn—in or the like, or a powder of a solder alloy such as Sb, bi, in, cu, zn, as, ag, cd, fe, ni, co, au, ge, P added to these alloys.

The solder alloy powder is preferably Pb-free solder.

Content of soldering flux:

in the solder paste according to the other embodiment, the content of the flux is preferably 5 to 30 mass%, more preferably 5 to 15 mass%, with respect to the total mass of the solder paste.

The solder paste according to this embodiment contains the flux according to this other embodiment, and thus sufficiently suppresses heat collapse. In addition, the generation of voids is sufficiently suppressed.

Examples

The present invention will be described below with reference to examples, but the present invention is not limited to the following examples.

< rosin >)

As the rosin, acrylic modified hydrogenated rosin, polymerized rosin, hydrogenated rosin are used.

< thixotropic agent >

As thixotropic agents, thixotropic agents a, B, bisamides, polyamides are used.

Thixotropic agent A: n, N' -bis (2-stearamidoethyl) -nonyldiamide

Thixotropic agent A is a compound represented by the following chemical formula (3-1).

[ chemical formula 6]

Thixotropic agent B: n, N' -bis (2-stearamidoethyl) -sebacamide

Thixotropic agent B is a compound represented by the following chemical formula (3-2).

[ chemical formula 7]

As the polyamide, a polyamide (PA 1)) obtained by the following method was used.

Preparation of Polyamide example 1

12-hydroxystearic acid and dodecanedioic acid were added and heated to about 100℃and then hexamethylenediamine was added and heated to about 220℃for 3 hours to give the polyamide of preparation 1.

Dodecanedioic acid used as a raw material was X mol, 12-hydroxystearic acid was Y mol, and hexamethylenediamine was Z mol. The number of moles of the raw material satisfies the relationship 2z=2x+y.

Preparation of Polyamide example 2

12-hydroxystearic acid and sebacic acid were added and heated to about 100℃and then hexamethylenediamine was added and heated to about 220℃for 3 hours to give the polyamide of preparation 2.

The sebacic acid used as a raw material was X moles, 12-hydroxystearic acid was Y moles, and hexamethylenediamine was Z moles. The number of moles of the raw material satisfies the relationship 2z=2x+y.

The temperature of the endothermic peak of the obtained polyamide was measured by DSC (Differential Scanning Calorimetry, differential scanning calorimeter).

As a more specific method for measuring the endothermic peak, it was measured by setting the temperature rise rate to 20℃per minute and raising the temperature of about 10mg of polyamide from 25℃to 350℃under a nitrogen atmosphere. As a measurement instrument, DSC7020 (hitachi high tech academy of sciences) was used. The measurement results are shown in FIG. 1. FIG. 1 is a graph showing a DSC curve of the polyamide-forming example 1 obtained. The temperature of the peak top is defined as the temperature of the endothermic peak.

The peak top temperature of all endothermic peaks of the obtained polyamide is 120 ℃ to 200 ℃.

As bisamide, ethylene bis stearamide (trade name: SLIPACKS E) was used.

< active agent >

As the organic acid, adipic acid, azelaic acid, glutaric acid are used.

As the halogen-based active agent, trans-2, 3-dibromo-2-butene-1, 4-diol is used.

As the amine, 2-phenylimidazole, 2-phenyl-4-methylimidazole was used.

< solvent >

As solvent diethylene glycol monohexyl ether was used.

< preparation of soldering flux >

Examples 1 to 15 and comparative examples 1 to 4

The respective fluxes of examples and comparative examples were prepared with the compositions shown in tables 1 to 3 below.

The content of each component in tables 1 to 3 is 100 mass% of the total mass of the flux, and the blank space is 0 mass%.

< preparation of solder paste >

The flux of each example and the solder alloy powder described below were mixed to prepare solder paste.

As the solder alloy powder, a sn—ag—cu-based solder alloy in which Ag is 3.0 mass%, cu is 0.5 mass%, and the balance Sn is used.

As the solder alloy powder, a solder alloy powder satisfying the size (particle size distribution) of symbol 4 in the classification of powder size in JIS Z3284-1:2014 (Table 2) was used.

The flux was set to 11 mass% and the solder alloy powder was set to 89 mass% for each of the prepared solder pastes.

< evaluation of print collapse >

Collapse of the solder paste upon printing was evaluated. The results are shown in tables 1 to 3.

The measuring method comprises the following steps:

the obtained solder paste was evaluated for print slump according to the method described in "slump test at printing" in JIS Z3284-3:2014. The test board was obtained by printing a solder paste using a metal mask provided with pattern holes shown as I (hole size 3.0×0.7) in fig. 6, which is configured with "collapse test at printing". For the test board, the minimum interval at which all of the printed solder paste cannot be integrated was evaluated.

< evaluation of Heat collapse >

The collapse of the solder paste obtained by mixing the flux and the solder alloy powder, respectively, upon heating was evaluated. The results are shown in tables 1 to 3.

The measuring method comprises the following steps:

the obtained solder paste was evaluated for heat collapse according to the method described in "collapse test under heat" in JIS Z3284-3:2014. First, a test board was obtained by printing a solder paste using a metal mask provided with pattern holes shown as I (hole size 3.0×0.7) in fig. 6 in which "collapse test at printing" was arranged. The test plate obtained was heated to 200℃in an air circulation type heating furnace. For the heated test board, the minimum interval at which all of the printed solder paste could not be integrated was evaluated.

Evaluation of heating collapse suppressing ability

Determination reference:

a: the evaluation value of the heat collapse is 0.5mm or less, or the difference between the evaluation value of the heat collapse and the evaluation value of the print collapse is 0.2mm or less.

B: the evaluation value of the heat collapse is 0.6mm or more, or the difference between the evaluation value of the heat collapse and the evaluation value of the print collapse is 0.3mm or more.

TABLE 1

TABLE 2

TABLE 3

As shown in example 1, a flux containing an acrylic modified hydrogenated rosin as a rosin, a thixotropic agent a and a polyamide (preparation example 1) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent can sufficiently suppress heat collapse.

As shown in example 2, a flux containing polymerized rosin, thixotropic agent a and polyamide (preparation 1) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 3, a flux containing hydrogenated rosin, thixotropic agent a and polyamide (preparation example 1) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 4, the flux containing the acrylic modified hydrogenated rosin as a rosin, the thixotropic agent a content was reduced, the polyamide (preparation example 1) contained, the adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 5, the flux containing the acrylic modified hydrogenated rosin as a rosin, increasing the content of the thixotropic agent a, containing the polyamide (preparation example 1), containing adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and containing diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 6, a flux containing an acrylic modified hydrogenated rosin as a rosin, a thixotropic agent B and a polyamide (preparation example 1) as a thixotropic agent for changing the types of thixotropic agents, and adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents and diethylene glycol monohexyl ether as a solvent can sufficiently suppress heat collapse.

As shown in example 7, the flux containing the acrylic modified hydrogenated rosin as a rosin, the thixotropic agent B content was reduced, the polyamide (preparation example 1) contained, the adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 8, the flux containing the acrylic modified hydrogenated rosin as a rosin, increasing the content of the thixotropic agent B, containing the polyamide (preparation example 1), containing adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and containing diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 9, a flux containing a thixotropic agent a and a polyamide (preparation example 1) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse by reducing the content of the acrylic acid-modified hydrogenated rosin.

As shown in example 10, the flux containing the thixotropic agent a and the polyamide (preparation example 1) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse by increasing the content of the acrylic acid-modified hydrogenated rosin.

As shown in example 11, a flux containing an acrylic modified hydrogenated rosin as a rosin, a thixotropic agent a, a thixotropic agent B and a polyamide (preparation example 1) as thixotropic agents, a reduced total content of the thixotropic agent a and the thixotropic agent B, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent can provide sufficient heat collapse suppressing ability.

As shown in example 12, a flux containing an acrylic modified hydrogenated rosin as a rosin, a thixotropic agent a, a thixotropic agent B and a polyamide (preparation example 1) as thixotropic agents, increasing the total content of the thixotropic agent a and the thixotropic agent B, containing adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and containing diethylene glycol monohexyl ether as a solvent was able to make the heat collapse suppressing ability sufficient.

As shown in example 13, the flux containing the acrylic modified hydrogenated rosin as rosin, the thixotropic agent a, the bisamide and the polyamide (preparation example 1) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as solvents was able to sufficiently suppress the heat collapse.

As shown in example 14, a flux containing an acrylic modified hydrogenated rosin as a rosin, a thixotropic agent a and a polyamide (preparation example 1) as thixotropic agents, glutaric acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

As shown in example 15, a flux containing an acrylic modified hydrogenated rosin as a rosin, a thixotropic agent a and a polyamide (preparation example 2) as thixotropic agents, adipic acid, azelaic acid, trans-2, 3-dibromo-2-butene-1, 4-diol, 2-phenylimidazole and 2-phenyl-4-methylimidazole as active agents, and diethylene glycol monohexyl ether as a solvent was able to sufficiently suppress heat collapse.

The fluxes of examples 1 to 14 contained the compound represented by the general formula (1) and polyamide (preparation example 1) and thus were able to sufficiently suppress the collapse by heating at 200 ℃.

The flux of example 15 can sufficiently suppress the collapse by heating at 200℃by containing the compound represented by the above general formula (1) and polyamide (preparation example 2). In contrast, the fluxes of comparative examples 1 and 4 did not contain the thixotropic agent a and the thixotropic agent B, and the heat collapse suppressing ability at 200 ℃ was insufficient.

In addition, the fluxes of comparative examples 2 and 3 did not contain polyamide (preparation example 1) or polyamide (preparation example 2), and the heat collapse suppressing ability at 200 ℃.

From these results, it is found that the heat collapse suppressing ability can be made sufficient by containing the compound represented by the general formula (1) and the polyamide.

The polyamide of preparation example 1 and the polyamide of preparation example 2 were prepared as follows. Using these polyamides, fluxes and solder pastes were prepared, and the occurrence of heat collapse and voids was evaluated.

As the polyamide, a polyamide (PA 2)) obtained by the following method was used.

Preparation of Polyamide example 1

Preparation of Polyamide example 2

< measurement of endothermic peak >

The temperature of the endothermic peak of the polyamides of preparation examples 1 and 2 was determined by DSC (Differential Scanning Calorimetry, differential scanning calorimeter).

As a more specific method for measuring the endothermic peak, the measurement was carried out by setting the temperature rise rate to 20℃per minute and heating about 7mg of the polyamides of production example 1 and production example 2 from 30℃to 220℃under a nitrogen atmosphere. As a measurement instrument, DSC7020 (hitachi high tech academy of sciences) was used. The temperature of the peak top is defined as the temperature of the endothermic peak.

The measurement results are shown in FIGS. 2 and 3.

FIG. 2 shows the endothermic peak of the polyamide of production example 1, and FIG. 3 shows the endothermic peak of the polyamide of production example 2.

< evaluation of Heat absorption ratio >

The proportions of the heat absorption amounts at a specific temperature of the polyamides prepared in preparation examples 1 and 2 were calculated as follows.

The heat absorption of the polyamide is calculated from the peak area of the DSC curve of the polyamide.

The "ratio of the amount of heat absorption at a specific temperature" means a ratio of the amount of heat absorption in a range of 50 ℃ or more and 200 ℃ or less to the total amount of heat absorption in a range of 50 ℃ or more and 200 ℃ or less. The results are shown in FIGS. 4 to 7.

Fig. 4 is a graph showing the relationship between the heat absorption amount ratio of the polyamide in production example 1 and the temperature, and fig. 5 is a graph showing the relationship between the heat absorption amount ratio of the polyamide in production example 2 and the temperature. FIG. 6 is a partially enlarged view of FIG. 4, showing the relationship between the heat absorption amount ratio and the temperature of the polyamide in preparation example 1.

The polyamide of preparation example 1 has a heat absorption rate of 90% or more at 190℃and a heat absorption rate of 98% or more at 195 ℃.

In contrast, the polyamide of preparation example 2 had a heat absorption at 190℃of less than 90% and a heat absorption at 195℃of less than 98%.

The heat absorption amount of the polyamide in production example 1 in the range of 195℃to 200℃is smaller than the heat absorption amount of the polyamide in production example 2 in the range of 195℃to 200 ℃.

< rosin >)

< thixotropic agent >

As thixotropic agents, the polyamides of preparation 1 and preparation 2, hexamethylenebishydroxystearamide, hydrogenated castor oil were used.

< active agent >

As the organic acid, adipic acid, suberic acid, hydrogenated dimer acid are used.

As amine, 2-phenylimidazole was used.

< solvent >

As solvent diethylene glycol monohexyl ether was used.

< preparation of soldering flux >

Test examples 1 to 14

The compositions shown in Table 4 below were prepared for each flux of the test examples.

The fluxes of test examples 1 to 13 contained rosin, a solvent, polyamide (PA 2), and an active agent.

The flux of test example 14 contained rosin, solvent and active agent, and did not contain polyamide (PA 2).

The content of each component in table 4 is the mass% when the total mass of the flux is 100 mass%, and the blank space is 0 mass%.

< preparation of solder paste >

< evaluation of Heat collapse >

The collapse of the solder paste obtained by mixing the flux and the solder alloy powder, respectively, upon heating was evaluated.

The measuring method comprises the following steps:

the obtained solder paste was evaluated for heat collapse according to the method described in "collapse test under heat" in JIS Z3284-3:2014. First, a test board was obtained by printing a solder paste using a metal mask having pattern holes shown as I (hole size 3.0×0.7) in fig. 6 and II (hole size 3.0×1.5) in fig. 6, which were arranged with "collapse test at printing". The test plate obtained was heated to 150℃or 200℃in an air-circulating heating furnace. For the heated test board, the minimum interval (in mm) at which all of the printed solder paste could not be integrated was evaluated. The results are shown in Table 4.

< evaluation of void Generation >

Solder paste was printed on a substrate (Cu-OSP treated glass epoxy substrate) using a metal mask (opening diameter: 0.30mm, mask thickness: 0.12 mm), and LGA (Land Grid Array: terminal treatment flash Au, pitch: 0.5mm, phi: 0.3mm, number of bumps: 160) was mounted.

Then, the temperature is raised to 40-150 ℃ at 3-4 ℃/s, maintained at 150-175 ℃ for 80-90 seconds, raised to 175-240 ℃ at 1-2 ℃/s, and maintained at 220 ℃ or more for 35-45 seconds by atmospheric reflow.

Then, the LGA mounting portion was photographed using an X-ray observation device (TUX-3200, manufactured by Shimadzu corporation). Data were acquired similarly for 3 LGAs (480 bumps total).

The ratio of the total area of the voids to the land area of the bump was calculated for each of the 480 bumps. The average value of the obtained ratio was calculated as the void area ratio. The results are shown in Table 4.

The ratio of the number of bumps having no void to the total number of bumps (480) was calculated and used as a void non-generation rate. The results are shown in Table 4.

Determination criterion of void area ratio:

a: the void area ratio is 1.2% or less.

B: the void area ratio exceeds 1.2%.

Determination criterion of void non-occurrence rate:

a: void non-occurrence rate is 35% or more.

B: void non-generation rate is less than 35%.

TABLE 4

Test examples 1 to 6 and 8 to 13 contained the polyamide of preparation example 1, and were sufficient in the ability to suppress heat collapse at 200 ℃.

Test example 14 contained no polyamide and had insufficient ability to suppress heat collapse at 200 ℃.

Test examples 1 to 12 contained the polyamide of preparation example 1, and were sufficient in the ability to suppress void generation.

Test example 13 contained the polyamide of preparation example 2, and was insufficient in the ability to suppress void generation.

The polyamide of preparation example 1 was prepared using dodecanedioic acid having 12 carbon atoms as a starting material.

The polyamide of preparation example 2 was prepared using sebacic acid having 10 carbon atoms as a starting material.

In general, the higher the number of carbon atoms in an organic compound such as a lipid, the higher the melting point thereof.

Surprisingly, the polyamide of production example 1 has a sufficiently high heat absorption rate in the range of 50℃to 190℃and a sufficiently high heat absorption rate in the range of 50℃to 195℃and therefore, the void generation suppressing ability is sufficient in test examples 1 to 12.

In addition, the polyamide of production example 2 was insufficient in the ability to suppress void generation in test example 13 because the proportion of heat absorption amount of 50 ℃ to 190 ℃ and the proportion of heat absorption amount of 50 ℃ to 195 ℃ were not sufficiently high.

Since the polyamide of preparation example 1 had a sufficiently high fluidity at 190℃and 195℃it was assumed that the void generation inhibition ability of test examples 1 to 12 was sufficient.

Since the polyamide of production example 2 does not have a sufficiently high fluidity at 190℃and 195℃it is assumed that the void generation suppressing ability of test example 13 is insufficient.

INDUSTRIAL APPLICABILITY

According to the present invention, it is possible to provide a flux and a solder paste which can sufficiently suppress heat collapse during reflow soldering. The flux and the solder paste can be applied to soldering of a substrate having a large area.

Claims

1. A soldering flux contains rosin, solvent, thixotropic agent and activator,

the thixotropic agent contains a compound represented by the following general formula (1) and a polyamide,

the polyamide is a condensate of an amine and at least one selected from aliphatic carboxylic acids and hydroxyl-containing aliphatic carboxylic acids, and has an endothermic peak temperature of 120 ℃ to 200 ℃ inclusive as measured by differential scanning calorimeter,

[ chemical formula 1]

Wherein R is ¹¹ Represents a hydrocarbon group having 11 to 30 carbon atoms which may have a substituent; r is R ^0a Represents a hydrocarbon group having 12 to 31 carbon atoms or a hydrogen atom which may have a substituent; r is R ^0b An n-valent hydrocarbon group having 4 to 12 carbon atoms which may have a substituent; r is R ²¹ An alkylene group having 2 to 6 carbon atoms; r is R ^0c An alkylene group having 2 to 6 carbon atoms or a single bond; n is 1 or 2; when n is 1, m is an integer of 1 to 3; when n is 2, m is 1.

2. The flux of claim 1 wherein the polyamide is a condensate of an aliphatic carboxylic acid, a hydroxyl-containing aliphatic carboxylic acid, and an amine.

3. A soldering flux according to claim 1 or claim 2 wherein the aliphatic carboxylic acid comprises a dicarboxylic acid.

4. The flux according to any one of claims 1 to 3, wherein the content of the compound represented by the general formula (1) is 1 mass% or more and 10 mass% or less with respect to the total mass of the flux.

5. The flux according to any one of claims 1 to 4, wherein the compound represented by the general formula (1) is a compound represented by the following general formula (3),

[ chemical formula 2]

Wherein R is ¹¹ And R is ¹¹ ' each independently represents a hydrocarbon group having 11 to 30 carbon atoms which may have a substituent; r is R ^0a And R is ^0a ' each independently represents a hydrocarbon group having 12 to 31 carbon atoms or a hydrogen atom which may have a substituent; r is R ^0b2 Represents a hydrocarbon group having 4 to 12 carbon atoms which may have a substituent; r is R ²¹ And R is ²¹ ' each independently represents an alkylene group having 2 to 6 carbon atoms; r is R ^0c And R is ^0c ' each independently represents an alkylene group having 2 to 6 carbon atoms or a single bond.

6. The flux of claim 5, wherein the compound represented by the general formula (3) is N, N '-bis (2-stearamidoethyl) -sebacamide or N, N' -bis (2-stearamidoethyl) -nonyldiamide.

7. The flux according to any one of claims 1 to 6, wherein the content of the rosin is 30 mass% or more and 50 mass% or less with respect to the total mass of the flux.

8. A solder paste comprising a solder alloy powder and the flux of any one of claims 1-7.