Year | Quantity| Value |Unit value
-------+---------+-----------+----------
| | |_Cents per_
|_Pounds_ | | _pound_
1919 |3,963,392| $1,190,984| 30.0
1920 |1,742,708| 429,116| 24.6
1923 |1,767,407| 318,765| 18.0
1924 |1,415,882| 237,639| 16.8
1925 |1,367,191| 282,078| 20.6
1926 | 767,698| 192,220| 25.0
1927 | 693,144| 143,700| 20.7
1928 |2,051,937| 259,100| 12.6
1929 |1,373,605| 197,986| 14.4
1930 | 607,690| 102,892| 16.9
1931 | 328,143| 48,095| 14.7
1932 | 260,339| 28,609| 11.0
1933 | ([1]) | ([1]) |
1934 | ([1]) | ([1]) |
1935 |3,353,625| 450,248| 13.4
1936 |1,146,026| 182,592| 15.9
1937[2]|1,375,036| 338,148| 24.6
-------+---------+-----------+----------
[1] Not reported separately.
[2] Preliminary.
Source: Foreign Commerce and Navigation of the United States.
Competitive conditions.
Glycerin occurs in chemical combination in animal and vegetable oils
and fats. Since it is obtained as a byproduct, the output is dependent
primarily upon the output of the major products, soaps and fatty acids,
and its production is largely independent of demand. At low prices,
however, less glycerin is recovered.
The United States usually consumes more glycerin than it produces (see
table 55), whereas leading European producing nations produce more than
they consume. In recent years the domestic production has apparently been
approaching domestic requirements. A factor tending to decrease demand
is the increasing resort to substitutes in various uses, particularly
ethylene glycol, ethyl alcohol, and methyl alcohol. On the other hand,
the demand in the resin industry is expanding rapidly.
TABLE 55.—_Refined glycerin: United States production, imports, exports,
and apparent consumption, in specified years_
-------+-------------+----------+----------+--------------
Year |Production[1]|Imports[2]|Exports[3]| Apparent
| | | |consumption[4]
-------+-------------+----------+----------+--------------
| _Pounds_ | _Pounds_ | _Pounds_ | _Pounds_
1927 | 108,392| 8,289| 693| 115,987
1929 | 125,772| 5,358| 1,374| 129,757
1931 | 113,894| 1,966| 328| 115,531
1932 | 105,163| 2,348| 260| 107,250
1933 | 104,120| 2,776| ([5]) | 106,895
1934 | 128,912| 2,214| ([5]) | 131,126
1935 | 123,390| 69| 3,354| 120,105
1936 | 132,922| 3,447| 1,146| 135,223
1937[6]| ([5]) | 7,535| 1,375| ([5])
-------+-------------+----------+----------+--------------
[1] From table 48 (refined basis).
[2] From table 51 (refined).
[3] From table 54 (grade not specified, but chiefly refined).
[4] Production plus imports minus exports.
[5] Not available.
[6] Preliminary.
Up to 1924 (except 1920) imports consisted principally of crude glycerin,
much of which was refined in the United States and included in United
States production; thereafter imports of refined glycerin became
important relative to the crude. Exports are insignificant compared to
either production or imports.
17. RAW MATERIALS FOR TAR-ACID RESINS
The first tar-acid resins were made from phenol and formaldehyde. As a
result this group of resins is frequently spoken of as phenolic resins.
This is true despite the fact that coal-tar acids other than phenol,
particularly the cresols and xylenols, are used in large volume today.
THE TAR ACIDS
The term coal-tar acids is applied to certain organic compounds either
obtained from or known to be present in coal tar. Probably the best known
is phenol or carbolic acid, produced in large quantities in the United
States and abroad. Others of commercial importance are ortho, meta,
and para cresol and the xylenols. All of these are definite chemical
compounds available as such or in mixture with other tar acids. Cresylic
acid is a term widely used in commerce for almost any mixture of tar
acids. Formerly it was used to designate a mixture of ortho, meta, and
para cresols in the proportions in which they are found in coal tar. The
higher boiling tar acids (listed in table 56 below the xylenols) have
little or no commercial importance at this time.
Table 56 lists the tar acids by commercial name, chemical name, boiling
point of the pure compound, and average percentage present in coal
tar. Boiling point is shown because the several tariff classifications
covering tar acids under the acts of 1922 and 1930 (pars. 27 and 1651)
depend upon distillation range (boiling points) for classification and
assessment of duty (see pp. 119 and 124).
TABLE 56.—_Tar acids: Commercial and chemical names, boiling points and
average percentage present in coal tar_
--------------------+-----------------------+---------+----------
| | | Average
Commercial name | Chemical name | Boiling |percent in
| |point ° C| coal tar
--------------------+-----------------------+---------+----------
Phenol |Phenol | 181.5| 0.7
Orthocresol |2-methyl phenol | 190.8| .4
Metacresol |3-methyl phenol | 202.8| .4
Paracresol |4-methyl phenol | 201.8| .3
2-3 Xylenol |2-3-dimethyl phenol | 218.0| ⎫
2-4 Xylenol |2-4-dimethyl phenol | 211.5| ⎪
2-5 Xylenol |2-5-dimethyl phenol | 211.5| ⎬ .2
2-6 Xylenol |2-6-dimethyl phenol | 212.0| ⎪
3-4 Xylenol |3-4-dimethyl phenol | 225.0| ⎪
3-5 Xylenol |3-5-dimethyl phenol | 220.0| ⎭
Ortho ethylphenol |2-ethyl phenol | 206.5| ⎫
Meta ethylphenol |3-ethyl phenol | 217.0| ⎪
Para ethylphenol |4-ethyl phenol | 218.5| ⎪
s-methyl ethylphenol|3-methyl-5-ethyl phenol| 232.5| ⎬ .5
Iso pseudocumenol |2-3-5-trimethyl phenol | 233.0| ⎪
Mesitol |2-4-6-trimethyl phenol | 219.5| ⎪
Pseudocumenol |2-4-5-trimethyl phenol | 234.0| ⎭
--------------------+-----------------------+---------+----------
Source: Ellis, Chemistry of Synthetic Resins.
Since the quantities of tar acids present in coal tar are small (see
table 56), it is usually uneconomical to distill coal tar completely
unless the creosote oil and pitch can be marketed profitably. Beginning
in 1936, production of tar acids in the United States was increased by
the practice of topping. Topping is the recovery in tar distillation of
the light fractions only, leaving a residual thin enough to flow through
the pipe lines to supply fuel to open hearth and other type furnaces.
These light fractions contain the naphthalene and tar acids. The practice
permits recovery of these products from tar to be used as fuel, thus
providing a new alternative intermediate between the two older practices
of either complete distillation or using the undistilled tar as fuel.
In the United States, consumption of most of the tar acids greatly
exceeds the quantities extracted from tar, necessitating large production
of synthetic phenol and importation of large quantities of the cresols
and xylenols. The calculated amount of these tar acids present in the tar
produced in this country vastly exceeds present day requirements. Table
57 shows the approximate amounts of the several tar acids contained in
the coal tar produced and distilled in 1936. These estimates are based on
a 1936 production of coal tar of 560,385,578 gallons and a distillation
of 292,140,249 gallons. The calculation is made by using the percentage
of tar acids in tar shown in table 56 and converting the gallons to
pounds in accordance with the specific weights of the pure tar acids.
Actual production of all tar acids in the United States in 1936 was about
29 million pounds.
TABLE 57.—_Tar acids available in coal tar produced and distilled in 1936_
-----------+--------------+--------------
| Available in | Available in
Tar acid | tar produced | tar distilled
| in 1936[1] | in 1936[2]
-----------+--------------+--------------
|_1,000 pounds_|_1,000 pounds_
Phenol | 34,912 | 18,200
Orthocresol| 19,277 | 10,050
Metacresol | 19,277 | 10,050
Paracresol | 14,290 | 7,450
Xylenols | 10,200 | 5,316
Others | 25,200 | 13,290
-----------+--------------+--------------
[1] 560,385,578 gallons.
[2] 292,140,249 gallons.
The several tar acids are discussed in detail under the following heads:
(_a_) Phenol.
(_b_) The cresols, xylenols, and cresylic acid.
(_c_) Synthetic tar acids other than phenol.
PHENOL
Description and uses.
Phenol (commonly called carbolic acid) is a tar acid obtained from two
sources: (_a_) From one of the fractions recovered in the distillation
of coal tar, a byproduct resulting from the manufacture of coke in
byproduct ovens, and from the manufacture of coal gas; (_b_) from
benzol, by synthesis. The second source has been the more important
since 1923. Phenol, when pure, is a colorless substance of interlaced
or separate needle-shaped crystals with a characteristic aromatic odor.
It is corrosive to the skin and to mucous membrane. When pure it is
water white, melts at about 42° C., and boils at about 181.5° C. It was
discovered in 1834 by Runge.
Phenol is used today chiefly as a component of tar-acid resins. It is
also widely used as an antiseptic and disinfectant, in the manufacture of
explosives (picric acid and ammonium picrate), and as an intermediate for
certain dyes and medicinals. Salicylic acid and its derivatives—aspirin,
salol, and methyl salicylate (artificial oil of wintergreen)—are
important medicinals made from phenol. Another use is in the extraction
of lubricating oils. The relative importance of these various uses in
recent years is indicated by table 58, which gives the estimated domestic
consumption of phenol by uses in 1936-37.
TABLE 58.—_Phenol: Estimated consumption by industries, 1936-37_
------------------------------+-----------------
Use |Percent of
|total consumption
------------------------------+-----------------
Synthetic resins | 60-65
Extraction of lubricating oil | 5
Insecticides and disinfectants| 10
Dyes and intermediates | 5
Other | 15-20
------------------------------+-----------------
United States production.
Prior to 1914 United States production of phenol averaged about a
million pounds a year and was entirely the natural product obtained from
distillates of coal tar. Increased demand during the World War was met
by several synthetic phenol processes, which utilized in part the vast
quantities of benzol available. Our output of phenol reached 64 million
pounds in 1917 and 107 million pounds in 1918. When the armistice was
signed stocks on hand in the United States totaled between 35 million and
40 million pounds, estimated at three times the annual consumption at
that time for nonmilitary purposes. As a result the price dropped from
about 45 cents to 6 cents a pound, and the synthetic plants were closed.
The limited quantities of phenol available to synthetic resin makers
prior to and during the World War caused much concern to that industry
and led to research work for substitutes, work resulting in the
development of many new and modified types of resins in which tar acids
other than phenol were used. But notwithstanding the use of these
other tar acids the increased demand for synthetic resins used up the
accumulated stocks of phenol sooner than was expected.
Of the phenol produced in the United States from 1919 through 1923 a
large part was natural phenol but the rapid increase in demand and the
improvement of processes for synthetic phenol had by 1923 resulted
in four companies beginning production of the synthetic article. The
rapid increase in output, from about 3 million pounds in 1923 to about
15 million pounds in 1925, was almost entirely in synthetic phenol.
Since then a large part of the domestic production has continued to be
synthetic, although the production of natural phenol since 1935 has been
about four times that of 1929.
Adequate quantities of coal tar are usually available to produce
sufficient natural phenol to meet a substantial part of our requirements,
if it were all recovered, but the quantity actually produced is
determined in part by the demand for other coal-tar products, and in part
by the value of the tar as fuel. More than 50 percent of the tar produced
has been burned as fuel, principally at the coke ovens or nearby steel
mills.
The domestic production and sales of phenol, natural and synthetic
combined, are shown in table 59.
TABLE 59.—_Phenol: United States production and sales, in specified
years, 1918-37_
-----------+----------+--------------------------------+---------------
|Production| Sales |
| | | Ratio of sales
Census year+----------+----------+----------+----------+ to total
| Quantity | Quantity | Value |Unit value| production
-----------+----------+----------+----------+----------+---------------
| _1,000 | _1,000 | _1,000 | | _Percent_
| pounds_ | pounds_ | dollars_ | |
1918 | 106,794 | 106,794 | 37,270 | $0.35 |
1919 | 1,544 | 1,544 | 156 | .10 |
1923 | 3,311 | 2,180 | 590 | .27 | 66
1925 | 14,734 | 8,524 | 1,771 | .21 | 58
1926 | 8,691 | 5,480 | 988 | .18 | 63
1927 | 8,041 | 4,595 | 684 | .15 | 57
1928 | 10,227 | 7,746 | 912 | .12 | 76
1929 | 24,178 | 19,939 | 2,248 | .11 | 83
1930 | 21,147 | 17,715 | 1,976 | .11 | 84
1931 | 17,981 | 14,002 | 1,446 | .10 | 78
1932 | 13,965 | 12,181 | 1,269 | .10 | 87
1933 | 33,220 | 27,923 | 2,881 | .10 | 84
1934 | 44,935 | 36,241 | 3,887 | .11 | 81
1935 | 43,419 | 34,575 | 3,431 | .10 | 80
1936 | 48,724 | 40,942 | 4,235 | .10 | 84
1937 | 65,690 | 57,176 | 6,153 | .11 | 87
-----------+----------+----------+----------+----------+---------------
Source: Compiled from annual reports of the Tariff Commission on
dyes and other synthetic organic chemicals in the United States.
_Grades produced for resins._—Increased production of phenol in recent
years is largely due to the demand from makers of synthetic resins. A
number of grades are regularly produced for this purpose, though it is
believed that the technical grade is the principal one used in resins.
The several grades are as follows:
(1) USP.—Either natural or synthetic. This grade contains not less than
98 percent phenol.
(2) Technical.—Various grades containing from 80 to 95 percent phenol, of
which the two most important are 82-84 percent and 90-92 percent.
(3) Mixtures.—Containing from 30 percent to 80 percent phenol and the
remainder of the isomeric cresols.
_Producers._—Natural phenol is obtained in the distillation of coal tar
and to a smaller extent in the purification of ammonia liquors in coke
and gas plants. In 1937 there were four producers of natural phenol with
plants located at Philadelphia, Pa., Follansbee, W. Va., Indianapolis,
Ind., and Pittsburgh, Pa. All these are tar distillers recovering
creosote oil, pitch, cresylic acid, naphthalene, and other crudes from
coal tar.
Synthetic phenol is made from benzene, either by sulfonation followed
by alkaline fusion, or by chlorination and subsequent heating under
pressure with caustic soda. It is produced in large quantities by two
firms, one at Midland, Mich., and the other at St. Louis, Mo. A third
producer is building a plant at North Tonawanda, N. Y., using a process
recently developed in Germany. Operation of this unit will probably start
late in 1938.
World production.
Natural phenol is recovered in practically all European countries and
in Japan. Germany and the United Kingdom are the principal producers
and have also been the leading exporters. Synthetic phenol was made in
Germany as early as 1900, and during the World War. Plants for synthetic
phenol recently installed are now in operation in Germany, Great Britain,
Belgium, and Italy.
Table 60 shows the average annual world production of phenol in recent
years by countries. Half of the total was produced in the United States.
TABLE 60.—_Phenol: Estimated average annual production, by countries,
1933-35_
--------------+-----------------
| Estimated
Produced in— |annual production
--------------+-----------------
| _1,000 pounds_
UNITED STATES | 41,000
United Kingdom| 18,000
Germany | 10,000
Poland | 3,000
Japan | 3,000
Czechoslovakia| 1,000
Belgium | 2,000
France | 2,000
Italy | 1,500
Spain | 700
+-----------------
Total | 82,200
--------------+-----------------
Source: Consular reports.
In the United Kingdom, where tar distillation is a well developed and
highly organized industry, large quantities of gas-works tar, rich in
phenol and other tar acids, are available. Prior to the World War the
United Kingdom was the principal source of phenol, and of the other
products of tar distillation. During the war several synthetic processes
of commercial importance were developed, but they were discontinued after
its close. A new synthetic unit has recently been installed in England
and is now in operation. Increasing consumption of phenol in synthetic
resins during the last decade, particularly in the last several years,
has changed the United Kingdom from an exporter to an importer of phenol.
Estimated consumption of phenol in the United Kingdom is given as 20
million pounds annually—principally in synthetic resins, and in lesser
quantities in dyes, intermediates, antiseptics, and disinfectants.
In Germany the phenol recovered in 1936 amounted to about 20 million
pounds, and recently three commercial units have been installed for the
production of synthetic phenol, one with a reported daily output of
11,000 pounds.
Natural phenol is also recovered in Belgium, France, the Netherlands,
Czechoslovakia, Poland, Italy, and Spain. Synthetic phenol has recently
been produced for the first time in Belgium and Italy. The quantities
normally produced in these countries are small and are supplemented by
imports from Great Britain and Germany.
The production of phenol in Japan has increased rapidly and has been
sufficient since 1930 to meet domestic requirements. The estimated output
increased from 300,000 pounds in 1927 to more than 3 million pounds
annually in recent years. The Miike Dyestuffs Works is reported to be
producing synthetic phenol.
United States imports.
_Rates of duty._—Prior to September 6, 1916, phenol was imported free of
duty. Since that date it has been dutiable at the various rates shown in
table 61. Under the act of 1930 the rate of duty is 3½ cents per pound
and 20 percent ad valorem on the American selling price (the wholesale
price of a similar competitive article manufactured in the United
States).[21]
TABLE 61.—_Phenol: Rates of duty upon imports into the United States,
1916-37_
------------------+------------------------+----------------------------
Period | Rate of duty | Authority
------------------+------------------------+----------------------------
To Sept. 8, 1916 |Free |Free under Tariff Act of
| | 1913 and previous acts.
| |
Sept. 9, 1916, to |2½ cents per pound plus |Under Revenue Act of 1916.
Sept. 21, 1922. | 15 percent ad valorem |
| on foreign value. |
| |
Sept. 22, 1922, to|7 cents per pound plus |Under par. 27 of Tariff Act
Sept. 21, 1924. | 55 percent ad valorem | of 1922; special provision
| on American selling | for first 2 years.
| price[1] or United |
| States value.[2] |
| |
Sept. 22, 1924, to|7 cents per pound plus |Under par. 27 of Tariff Act
Nov. 29, 1927. | 40 percent ad valorem | of 1922, rate provided
| on American selling | for period after the
| price[1] or United | first 2 years.
| States value.[2] |
| |
Nov. 30, 1927, to |3½ cents per pound plus |By Presidential proclamation
June 17, 1930. | 20 percent ad valorem | following a cost of
| on American selling | production investigation
| price[1] or United | under sec. 315 of Tariff
| States value.[2] | Act of 1922.
| |
June 18, 1930 |3½ cents per pound plus |Under par. 27 (b) of Tariff
| 20 percent ad valorem | Act of 1930.
| on American selling |
| price[3] or United |
| States value.[4] |
------------------+------------------------+----------------------------
[1] As defined in subdivision (f) of section 402, title IV, act
of 1922.
[2] As defined in subdivision (d) of section 402, title IV, act
of 1922.
[3] As defined in subsection (g) of section 402, title IV, act of
1930.
[4] As defined in subsection (e) of section 402, title IV, act of
1930.
_Import statistics._—Imports for consumption are shown in tables 62
and 63. Table 62 shows imports of phenol or carbolic acid and table 63
imports of “all distillates of tars yielding below 190° C. an amount of
tar acids equal to or more than 5 percent.” Imports under the latter
classification prior to 1928 were probably chiefly phenol. Phenol imports
consist entirely of the natural product.
TABLE 62.—_Phenol: United States imports for consumption, 1910-37_
-------+----------------------+---------+--------+----------+----------
| | | | | Computed
Year | Rate of duty | Quantity| Value |Unit value|ad valorem
| | | | | rate
-------+----------------------+---------+--------+----------+----------
| | _Pounds_| | | _Percent_
1910[1]|Free |4,507,693|$275,600| $0.061|
1911[1]| do |4,371,014| 265,780| .061|
1912[1]| do |5,686,704| 521,457| .092|
1913[1]| do |8,345,631| 688,771| .083|
1914[1]| do |8,393,216| 531,535| .063|
1915[1]| do |3,106,445| 179,685| .058|
1916[1]|([2]) |2,246,256| 154,841| .069|
1917[1]|15 percent + 2½ cents | 265,519| 17,168| .065| 53.7
| per pound | | | |
1918 | do | 283,337| 62,497| .221| 26.3
1919 | do | 2,061| 264| .128| 34.5
1920 | do | 1,040| 244| .235| 25.8
1921 | do | 250| 142| .568| 19.4
1922 |([3]) |} 280,224| 30,414| .109| 38.0
| |} 69,310| 16,102| .230| 85.1
1923 |55 percent + 7 cents | 126,618| 21,389| .169| 96.4
| per pound [4] | | | |
1924 |([5]) | 176,081| 46,786| .266| 81.4
1925 |40 percent + 7 cents | 256,126| 58,958| .230| 70.4
| per pound [4] | | | |
1926 | do | 218,437| 47,351| .217| 72.3
1927 |([6]) | 500| 100| .200| 75.0
1928 |20 percent + 3½ cents | 1,653| 298| .180| 39.4
| per pound [4] | | | |
1929 | do | 433,385| 44,226| .102| 54.3
1930 | do | 500| 115| .230| 39.4
1931 | do | 2,365| 639| .270| 33.0
1932 | do | None| | |
1933 | do | 3,440| 641| .186| 38.8
1934 | do | None| | |
1935 | do | 2,605| 211| .081| 63.0
1936 | do | 71,429| 8,302| .116| 50.1
1937[7]| do | 32,238| 3,767| .117| 50.0
-------+----------------------+---------+--------+----------+---------
[1] Fiscal year.
[2] 15 percent ad valorem and 2½ cents per pound effective Sept.
9, 1916.
[3] 55 percent ad valorem and 7 cents per pound, effective Sept.
22, 1922.
[4] Ad valorem based on American selling price or United States
value under acts of 1922 and 1930.
[5] Ad valorem reduced to 40 percent effective Sept. 22, 1924.
[6] Duty reduced to 20 percent ad valorem and 3½ cents per pound
effective Nov. 30, 1927.
[7] Preliminary.
Source: Foreign Commerce and Navigation of the United States.
TABLE 63.—_All distillates of tar yielding below 190° C. an amount of
tar acids equal to or more than 5 percent: United States imports for
consumption, 1918-37_
---------+----------------------+--------+------+----------+----------
| | | | | Computed
Calendar | Rate of duty |Quantity| Value|Unit value|ad valorem
year | | | | | rate
---------+----------------------+--------+------+----------+----------
| |_Pounds_| | | _Percent_
1918 |15 percent + 2½ cents | 1,550|$2,008| $1.30| 16.93
| per pound | | | |
1919 | do | 3,170| 4,587| 1.45| 16.73
1920 | do | 85,474|36,041| .422| 20.93
1921 | do | 16,240|11,811| .727| 18.43
1922 |([1]) | 350,764|42,912| .122| 46.27
1923 |55 percent + 7 cents | 245,119|30,328| .124| 111.58
| per pound[2] | | | |
1924 |([3]) | 662,938|49,380| .074| 134.43
1925 |40 percent + 7 cents | 252,382|15,441| .061| 154.41
| per pound[2] | | | |
1926 | do | 1,102| 5,236| 4.75| 41.47
1927 |([4]) | 2| 16| 8.00| 40.88
1928-37 | | None| | |
---------+----------------------+--------+------+----------+----------
[1] 55 percent ad valorem and 7 cents per pound, effective Sept.
22, 1922.
[2] Ad valorem based on American selling price or United States
value under acts of 1922 and 1930.
[3] Ad valorem reduced to 40 percent, effective Sept. 22, 1924.
[4] Duty reduced to 20 percent ad valorem and 3½ cents per pound,
effective Nov. 30, 1927.
Source: Foreign Commerce and Navigation of the United States.
United States exports.
Exports of phenol have not been separately shown in official statistics
since 1924. In that year they went chiefly to Panama, Japan, Cuba, and
Mexico. Table 64 shows exports from 1918 to 1924, inclusive, as furnished
by the Department of Commerce.
TABLE 64.—_Phenol: United States exports, 1918-24_
----+---------+----------+----------
Year| Quantity| Value |Unit value
----+---------+----------+----------
| _Pounds_| |
1918|6,477,841|$2,666,634| $0.412
1919|1,243,841| 363,744| .292
1920|2,151,475| 388,047| .180
1921| 249,658| 35,994| .144
1922| 223,146| 23,223| .104
1923| 232,830| 34,389| .148
1924| 51,364| 8,016| .156
----+---------+----------+----------
Source: Commerce and Navigation of the United States.