Appreciable quantities of phenol have been exported in recent years to

Japan and China, and to Great Britain and other European countries.

Export statistics, collected by the U. S. Tariff Commission from the

several domestic producers, show the following quantities exported in

recent years.

TABLE 65.—_Phenol: United States exports, 1934-36_

----+---------+--------+----------

Year| Quantity| Value |Unit value

----+---------+--------+----------

| _Pounds_| |

1934|2,622,900|$329,269| $0.126

1935|2,921,835| 322,933| .111

1936|1,258,244| 148,501| .118

----+---------+--------+----------

Source: Data obtained by the U. S. Tariff Commission through

questionnaires.

In 1934, the principal destinations in order of importance were China,

Italy, and Canada; in 1935 Germany, China, Japan, and Belgium; and in

1936 China, Belgium, and the Netherlands.

Competitive conditions.

Before the World War our average annual consumption of phenol was 5

million pounds, of which about 80 percent was imported from Great

Britain and Germany. These countries produced phenol in excess of their

consumption, and phenol was on the free list in the United States.

In September 1916 phenol became dutiable. The demand was increasing

rapidly because of the use of phenol in the manufacture of picric acid,

an explosive. To meet the wartime demand at home and abroad large scale

production of synthetic phenol sprang up in the United States. But the

end of the war not only shut off the largest part of the demand but left

the producers with large stocks on hand. The price dropped sharply and

the production of synthetic phenol ceased.

Since 1922 there has been a gradually increasing demand for phenol in the

United States, chiefly for use in the manufacture of synthetic resins,

and production has increased to meet this demand as shown in table 66.

TABLE 66.—_Phenol: United States production, imports, exports, and

apparent consumption in specified years, 1918-37_

[In thousands of pounds]

----+-------------+----------+----------+---------------

Year|Production[1]|Imports[2]|Exports[3]| Apparent

| | | |consumption[4]

----+-------------+----------+----------+---------------

1918| 106,794| 285| 6,478| ([5])

1919| 1,544| 5| 1,244| ([5])

1923| 3,311| 372| 233| 3,450

1925| 14,734| 919| ([6]) | ([7])

1926| 8,691| 220| ([6]) | ([7])

1927| 8,041| 1| ([6]) | ([7])

1928| 10,227| 2| ([6]) | ([7])

1929| 24,178| 433| ([6]) | ([7])

1930| 21,147| 1| ([6]) | ([7])

1931| 17,981| 2| ([6]) | ([7])

1932| 13,965| | ([6]) | ([7])

1933| 33,220| 3| ([6]) | ([7])

1934| 44,935| | 2,623| 42,312

1935| 43,419| 3| 2,922| 40,500

1936| 48,724| 71| 1,258| 47,537

1937| 65,690| 32| ([6]) | ([7])

----+-------------+----------+----------+---------------

[1] From table 59.

[2] From tables 62 and 63.

[3] From tables 64 and 65.

[4] Production plus imports minus exports.

[5] Not calculated because of importance of stocks on hand.

[6] Not available.

[7] Not available because of absence of export figures. Exports

probably negligible up to 1929; substantial in 1933.

The manufacture of synthetic phenol was revived about 1923. Imports were

quite small as compared with production, especially after 1927. At first

this was probably due primarily to the protection given by the duty

which had been increased in 1922.[22] But with the increase in volume of

production in the United States the price decreased and since 1933 the

United States producers have enjoyed a substantial export business. It

may therefore be doubted that in recent years there would have been any

substantial imports even if phenol had been free of duty.

THE CRESOLS, XYLENOLS, AND CRESYLIC ACID

Reference to table 56, page 109, will show that, as distillation of coal

tar proceeds and the temperature of distillation is increased, the phenol

fraction is followed in order by the three cresols and then by the six

xylenols. Each of these tar acids is a definite chemical compound with

definite physical properties. Consideration of them as raw materials

for synthetic resins is complicated by the fact that they are generally

used in mixtures and that the commercial term, cresylic acid, applied

to many of these mixtures has no definite relationship to the precise

chemical terminology. Yet since the term cresylic acid is so widely used

in commerce, since the tariff provides for imports under that name, and

since the statistics available are in part in terms of cresylic acid and

in part in terms of cresols and xylenols it is impossible to present the

complete picture on the basis of the correct chemical terminology.

Description and uses.

_The cresols._—The cresols are isomeric tar acids obtained from coal

tar by fractional distillation. Their combined content averages about

1 percent of domestic coal tar. The total cresol content is divided in

about the following proportions: 40 percent metacresol, 35 percent

orthocresol, and 25 percent paracresol. The cresols are marketed in a

number of types and grades including mixtures of ortho, meta, and para;

mixtures of meta and para; separated ortho, meta, and para; and also in

mixtures with phenol and the xylenols.

_Metacresol_ (chemically, 3-methyl phenol) is a colorless to yellow

liquid with a phenol-like odor. When pure, it melts at 11° C., boils

at 202.8° C., and has a specific gravity of 1.03. It is used in the

manufacture of synthetic resins, photographic developers, explosives,

disinfectant soaps, paint and varnish removers, to remove ink from

newsprint, to soften and reclaim rubber, and in intermediates for dyes

and perfume materials.

_Orthocresol_ (chemically, 2-methyl phenol) is a colorless, crystalline

product with a phenol-like odor, melting at 30° C., boiling at 190.8° C.,

and having a specific gravity of 1.04. It is used in the manufacture of

coumarin (flavor), antiseptics, disinfectants, and fumigants. It is not

used to any extent in synthetic resins.

_Paracresol_ (chemically, 4-methyl phenol) is a colorless, crystalline

substance with a phenol-like odor, melting at 35° C., boiling at 201.8°

C., and having a specific gravity of 1.03. It is used in the manufacture

of intermediates, dyes, disinfectants, and fumigants, in medicine, and

in mixture with metacresol in synthetic resins. Domestic production

of synthetic paracresol was announced early in 1938 by Swann & Co.,

Birmingham, Ala.

_Metaparacresol_ is a combination of approximately 60 percent meta

and 40 percent para cresol obtained in the fractional distillation of

mixed cresols. The ortho isomer is distilled off, leaving a residue of

metaparacresol. It is widely used in the manufacture of synthetic resins.

_Cresol._—The term cresol used without further qualification indicates

a mixture of the three isomers in substantially the same proportions

in which they are found in coal tar. The United States Pharmacopoeia

describes cresol, a mixture of isomeric cresols obtained from coal tar,

as a colorless or yellowish to brownish-yellow or a pinkish, highly

refractive liquid, becoming darker with age and on exposure to light. It

is widely used in synthetic resins, antiseptics and disinfectants, and in

medicine.

_The xylenols._—Shortly after the original patents on Bakelite resins

expired extensive research was begun for raw materials that would give

different properties to the resultant resins. This work led to a study of

the high-boiling tar acids, and methods of recovery for some of them were

commercially developed. Among those obtained from coal tar are the six

isomeric xylenols, methylethyl phenol, and one of the trimethyl phenols

(see table 56). Coal tar contains about 0.2 percent xylenols and 0.5

percent other high-boiling tar acids.

The principal uses for these products have been in the preparation of

high-phenol coefficient disinfectants, and recently in the replacement

of phenol and cresols in synthetic resins. It was found, for example,

that 3: 5 xylenol reacts with formaldehyde faster than either metacresol

or phenol. Numerous patents have been granted on the use of these

high-boiling acids in the production of synthetic resins.

The xylenols, when pure, are colorless, crystalline substances boiling

between 211° and 225° C. They are usually marketed in mixtures containing

from 50 to 80 percent xylenols and 20 to 50 percent cresols. There is

commercial production of at least one of the separated xylenols (3: 5).

An appreciable part of our imports of crude cresylic acid and of our

production of cresylic acid contains high percentages of the xylenols.

_Other high-boiling tar acids._—The other high-boiling tar acids

are ortho ethylphenol, meta ethylphenol, para ethylphenol, methyl

ethylphenol, and the three isomeric trimethyl phenols. Several of these

have been isolated from coal tar. All of them, when pure, are crystalline

compounds with boiling points ranging between 206° and 235° C. There

has been little, if any, commercial production of this group up to this

time. They are known, however, to have very high phenol coefficients, a

property which would make them suitable for use in disinfectants. Little

is known as yet concerning their application in synthetic resins.

_Cresylic acid._—Cresylic acid is a generic term now applied to mixtures

of tar acids in widely varying proportions. As defined in the literature

and as formerly used in commerce the term identified a mixture of

ortho, meta, and para cresols in the proportions in which they occur in

coal tar. This proportion is approximately 40 percent metacresol, 35

percent orthocresol, and 25 percent paracresol. But in recent years the

designation cresylic acid has been applied to all sorts of mixtures of

tar acids boiling above 190° C. Practically every maker of synthetic

resins, antiseptics, and disinfectants has his own specifications for

cresylic acid; it may be any mixture in almost any proportions of the

three cresols, the six isomeric xylenols, and the higher boiling tar

acids. Imports of crude cresylic acid are understood to be largely

xylenol mixtures containing low percentages of the cresols. This loose

application of cresylic acid in recent years is due to the increased

commercial application of the high-boiling tar acids, especially the

xylenols.

Under the Tariff Act of 1930 refined cresylic acid, that having a purity

of 75 percent or more, is dutiable under paragraph 27 at 3½ cents per

pound and 20 percent ad valorem based on American selling price or United

States value; while crude cresylic acid, that having a purity of less

than 75 percent, is free under paragraph 1651. The provision in paragraph

27 reads, “cresylic acid which on being subjected to distillation

yields in the portion distilling below two hundred and fifteen degrees

centigrade, a quantity of tar acids equal to or more than 75 per centum

of the original distillate.” Under this provision cresylic acid may

include an endless number of combinations of tar acids and may or may not

contain any of the isomeric cresols. Of the 17 or more tar acids known

to exist in coal tar (see table 56), only 8 have boiling points above

215° C. It would seem to be more accurate and more in line with present

day usage to have the tariff drop the designation cresylic acid in favor

of more definite terms based on composition, such as cresols and cresol

mixes, xylenol and xylenol mixes, etc.

About 60 percent of our consumption of cresylic acid is in synthetic

resins and the remainder in the manufacture of insecticides, antiseptics,

disinfectants, and other coal-tar products, such as intermediates for

dyes, plasticizers for nitrocellulose, etc.

United States production.

_The cresols._—There is large production of cresol, metaparacresol, and

orthocresol in the United States. Commercial production of paracresol was

reported for the first time in 1934, and of metacresol in 1935.

Statistics of domestic production and sales are publishable only for the

year 1934 because of the small number of producers. The output in that

year is shown in table 67. Production has increased appreciably since

then.

TABLE 67.—_Meta, ortho, and para cresols: United States production and

sales, 1934_

----------------+------------+-----------------------------------

| | Sales

Type | Production +-----------+----------+------------

| | Quantity | Value | Unit value

----------------+------------+-----------+----------+------------

| _Pounds_ | _Pounds_ | |

Cresol | 8,929,836 | 8,559,048 | $572,738 | $0.07

Metaparacresol | 2,033,424 | 1,692,149 | 101,324 | .06

Orthocresol | 835,016 | ([1]) | ([1]) |

Paracresol | ([1]) | ([1]) | ([1]) |

----------------+------------+-----------+----------+------------

[1] Not publishable; figures would reveal operations of

individual firms.

Source: Dyes and Other Synthetic Organic Chemicals in the United

States. U. S. Tariff Commission.

The trend of domestic production of the several cresols is upward. In

1937 the output of all grades and types of cresols was 13,745,271 pounds

with sales of 13,251,345 pounds, valued at $1,071,965. The practice of

topping coal tar will greatly increase the output of the cresols as well

as of other tar acids and naphthalene.

There are five domestic producers of cresol, three each of orthocresol

and metaparacresol, and two of metacresol and paracresol. All except one

of these makers recover natural phenol, cresylic acids, and other tar

acids. Refining plants are located at Pittsburgh, Pa., Philadelphia,

Pa., Indianapolis, Ind., and Follansbee, W. Va. Domestic production of

synthetic paracresol was first announced in 1938.

_The xylenols._—There has been a large domestic production of mixed

xylenols in recent years. These mixtures, containing from 50 to 80

percent xylenols, are marketed as cresylic acid. Statistics of domestic

production, and sales are therefore included in table 68. It is estimated

that the output of xylenols and xylenol mixtures in 1935 exceeded 750,000

pounds and exceeded 1,250,000 pounds in 1937. At least one of the

separated xylenols (1: 3: 5) has been produced commercially in the United

States since 1935, but statistics of its production are not publishable.

_Other high-boiling tar acids._—There was no reported domestic production

of the other high-boiling acids prior to 1935 and the data obtained for

that year are probably incomplete. Estimated output was 200,000 pounds in

1935, 250,000 pounds in 1936, and 300,000 pounds in 1937. These estimates

are based on production of mixtures of high-boiling acids.

_Cresylic acid._—Domestic production and sales statistics for so-called

crude cresylic acid are not publishable. It is known, however, that

production of the crude is small compared with our output of refined

cresylic acid. It is usually more economical for the producer to prepare

the mixture of tar acids to the specifications of the purchaser, rather

than to leave part of the refining operations to be performed by the

latter. The fact that imports of cresylic acid are chiefly of crude is

largely due to the different tariff treatment of crude and refined.

Domestic production of refined cresylic acid was confined to one or two

firms until 1928, when there were four makers. Statistics of production

and sales are not publishable for the years prior to 1929, though it may

be stated that the annual domestic output increased each year to supply

the increased demand. Table 68 shows production and sales from 1929 to

1934, inclusive. Data for later years are not publishable.

TABLE 68.—_Refined cresylic acid: United States production and sales,

1929-37_

-----+------------+-------------------------------------

| | Sales

Year | Production +------------+------------+-----------

| | Quantity | Value | Unit value

-----+------------+------------+------------+-----------

| _Pounds_ | _Pounds_ | | _Per pound_

1929 | 14,601,534 | | | $0.10

1930 | 17,305,308 | 16,026,407 | $1,267,155 | .08

1931 | 10,994,000 | 10,305,000 | 652,000 | .06

1932 | 8,060,000 | 4,805,000 | 251,000 | .05

1933 | 13,813,941 | 11,975,441 | 626,496 | .05

1934 | 10,949,860 | 9,230,255 | 489,231 | .05

1935 | ([1]) | ([1]) | ([1]) |

1936 | ([1]) | ([1]) | ([1]) |

1937 | ([1]) | ([1]) | ([1]) |

-----+------------+------------+------------+-----------

[1] Not publishable; figures would reveal operations of

individual firms.

Source: Compiled from annual reports of the Tariff Commission on

dyes and other synthetic organic chemicals in the United States.

As previously stated, the composition of cresylic acid has gradually been

changed from a mixture of the isomeric cresols to mixtures of cresols,

xylenols, and high-boiling tar acids. The cresols, formerly included

under cresylic acid statistics, are now shown separately. For this reason

the data in table 68 do not fully reflect the increased output of these

tar acids in recent years. Statistics for years prior to 1931 probably

include all of the tar acids except phenol, while those for subsequent

years do not include the separated cresols. In 1934 the production of

refined cresylic acid was 10,949,860 pounds, and in addition recovery

of the several cresols amounted to 11,798,276 pounds making a total of

22,748,136 pounds as compared with a total of 14,601,534 pounds in 1929

and 17,305,308 pounds in 1930.

During 1936 and the first part of 1937 a serious shortage of cresylic

acid existed in the domestic market owing to increased demand by

synthetic resin makers. The output in 1936 exceeded that in 1935 and

the production in 1937 was appreciably higher than in 1936. These

increases are due to the recovery of appreciable quantities at several

new distillation plants, the topping of large amounts of tar hitherto not

processed, and increased production by present recovery units.

There are many grades of cresylic acid, most of which are prepared by

mixing or blending to individual specifications. Every large consumer

apparently has his own specifications. In addition to these special

mixtures there are the following standard blends:

(1) Ninety-nine percent high-boiling, straw color.

(2) Low-boiling, straw color.

(3) Special resin grade, high-boiling.

There are four domestic producers of cresylic acid with recovery and

refining units at Pittsburgh, Pa., Philadelphia, Pa., Indianapolis,

Ind., and Follansbee, W. Va. The last three mentioned are refining

plants operated in conjunction with a number of tar distillation units

widely scattered throughout the country. These units usually recover

crude tar-acid fractions in the distillation of tar and ship them to

these refining plants for separation and refining. All in this group are

purchasers of coal tar. The fourth producer operates a byproduct recovery

unit in connection with the company’s coke-oven operations. Part of the

coal tar produced is distilled to recover the several products, including

creosote oil, tar acids, and naphthalene, and the residual pitch is mixed

with the remaining undistilled tar and used for fuel. The shortage of tar

acids and naphthalene in 1936 caused this producer to begin the topping

of tar.

Foreign production.

The cresols are produced in the United Kingdom, Germany, France, the

Netherlands, Belgium, and other European countries. Coal tar recovered

in the United Kingdom is principally gas tar, which is much richer in

tar acids than coke-oven tar, the principal source in the United States.

This is true because low temperature carbonization of coal yields greater

quantities of tar acids than are obtained in the tar from byproduct coke

ovens. Exports to the United States are chiefly mixtures which can enter

as crude cresylic acid.

Production of cresol in Germany in recent years is shown in table 69.

TABLE 69.—_Cresol: German production, in specified years_

-------+------------

Year |1,000 pounds

-------+------------

1929 | 23,814

1931[1]| 15,435

1933 | 11,780

1934 | 10,476

-------+------------

[1] Includes 2,866,000 pounds of separated ortho, meta, and para

cresols.

Source: Consular reports.

German imports and exports of cresol, in recent years, are shown in table

70.

TABLE 70.—_Cresol: German imports and exports, in specified years_

----+--------+--------

Year|Imports |Exports

----+--------+--------

|_1,000 |_1,000

| pounds_| pounds_

1929| 2,037 | 8,494

1930| 1,277 | 6,712

1931| 1,874 | 7,980

1932| 1,541 | 3,669

1933| 1,832 | 4,970

1934| 1,960 | 6,345

1935| 2,117 | 8,528

1936| 3,737 | 4,531

1937| 1,787 | 4,423

----+--------+--------

Source: Consular reports (1929-33) and official German statistics

(1934-37).

The output of cresols in Czechoslovakia in recent years is shown in table

71.

TABLE 71.—_Cresol: Production in Czechoslovakia, in specified years_

-----+----------

Year | Quantity

-----+----------

| _1,000

| pounds_

1928 | 1,984

1931 | 1,477

1932 | 1,102

1933 | 1,599

1934 | 1,918

-----+----------

Source: Consular reports.

Cresylic acid is recovered in all the countries of Europe, Great Britain

and Germany being the leading producers and the principal exporters.

Increasing demand in these countries for synthetic resins made from

cresylic acid has greatly reduced the quantities available for export in

recent years.

Great Britain is probably the world’s largest producer of cresylic acid,

and for many years has been the principal exporter to the United States.

This position is due to the large available supply of gas-house tar, and

to an ample market for all the products of tar distillation. In 1935

the tar distilled in England, Wales, and Scotland totaled 360 million

gallons, of which 55 percent was gas-house tar.

British production of all grades of cresylic acid averages between 35

million and 42 million pounds annually, of which from 12 million to 20

million pounds are exported. Many British producers market their tar

products through pools and associations. There is a cresylic acid pool, a

phenol pool, and at least two creosote oil export associations, a pitch

marketing association, and a benzol association. One of the principal

grades of cresylic acid produced in Great Britain is “American duty-free

specification.”

Table 72 shows British exports of cresylic acid, by countries, in recent

years.

TABLE 72.—_Cresylic acid: British exports, by countries, 1933-37_

-------------------+------+------+------+------+------

Destination | 1933 | 1934 | 1935 | 1936 | 1937

-------------------+------+------+------+------+------

| Quantity (in thousands of pounds)

+------+------+------+------+------

UNITED STATES | 3,616| 5,783| 6,116|11,296|([1])

Chile | 1,381| 2,958| 2,814| 662|([1])

France | 358| 87| 214| 189|([1])

Japan | 632| 203| 685| 2,002|([1])

All other countries| 5,464| 6,965| 7,333| 9,250|([1])

+------+------+------+------+------

Total |11,451|15,997|17,162|23,399|26,697

+------+------+------+-------------

| Value (in thousands of dollars)

+------+------+------+------+------

UNITED STATES | 147| 277| 255| 620|([1])

Chile | 28| 89| 87| 31|([1])

France | 21| 5| 20| 14|([1])

Japan | 38| 20| 43| 118|([1])

All other countries| 189| 307| 330| 537|([1])

+------+------+------+------+------

Total | 422| 698| 734| 1,321| 2,262

-------------------+------+------+------+------+------

[1] Not available.

Source: Official British statistics.

Imports into the United States.

_Rates of duty._—Prior to September 8, 1916, the cresols were imported

free of duty. Since that date they have been subject to the tariff

treatment shown in table 73.

TABLE 73.—_The cresols: Rates of duty upon United States imports, 1916-37_

Synthetic resins and their raw materials A survey of the types and uses of synthetic resins, the organization of the industry, and the trade in resins and raw materials, with particular references to factors essential to tariff consideration. Under the general provisions of section 332, title III, part II, Tariff act of 1930. · 第 16 / 22 段