and thenceforth the _Genius_ was published weekly, under the joint
editorship of the two men. It was understood, however, that Garrison
would do most of the editorial work, while Lundy would spend most of his
time in lecturing and procuring subscribers. On one point the two
editors differed radically, Lundy being the advocate of gradual and
Garrison of immediate emancipation. The former was possessed with the
idea that the negroes, on being emancipated, must be colonized somewhere
beyond the limits of the United States; the latter held that they should
be emancipated on the soil of the country, with all the rights of
freemen. In view of this difference it was agreed that each should speak
on his own individual responsibility in the paper, appending his initial
to each of his articles for the information of the reader. It deserves
mention here that Garrison was then in utter ignorance of the change
previously wrought in the opinions of English abolitionists by Elizabeth
Heyrick's pamphlet in favour of immediate, in distinction from gradual
emancipation. The sinfulness of slavery being admitted, the duty of
immediate emancipation to his clear ethical instinct was perfectly
manifest. He saw that it would be idle to expose and denounce the evils
of slavery, while responsibility for the system was placed upon former
generations, and the duty of abolishing it transferred to an indefinite
future. His demand for immediate emancipation fell like a tocsin upon
the ears of slaveholders. For general talk about the evils of slavery
they cared little, but this assertion that every slave was entitled to
instant freedom filled them with alarm and roused them to anger, for
they saw that, if the conscience of the nation were to respond to the
proposition, the system must inevitably fall. The _Genius_, now that it
had become a vehicle for this dangerous doctrine, was a paper to be
feared and intensely hated. Baltimore was then one of the centres of the
domestic slave trade, and upon this traffic Garrison heaped the
strongest denunciations. A vessel owned in Newburyport having taken a
cargo of slaves from Baltimore to New Orleans, he characterized the
transaction as an act of "domestic piracy," and avowed his purpose to
"cover with thick infamy" those engaged therein. He was thereupon
prosecuted for libel by the owner of the vessel, fined $50, mulcted in
costs, and, in default of payment, committed to gaol. His imprisonment
created much excitement, and in some quarters, in spite of the
pro-slavery spirit of the time, was a subject of indignant comment in
public as well as private. The excitement was fed by the publication of
two or three striking sonnets, instinct with the spirit of liberty,
which Garrison inscribed on the walls of his cell. One of these,
_Freedom of Mind_, is remarkable for freshness of thought and terseness
of expression.
John G. Whittier, the Quaker poet, interceded with Henry Clay to pay
Garrison's fine and thus release him from prison. To the credit of the
slaveholding statesman it must be said that he responded favourably, but
before he had time for the requisite preliminaries Arthur Tappan, a
philanthropic merchant of New York, contributed the necessary sum and
set the prisoner free after an incarceration of seven weeks. The
partnership between Garrison and Lundy was then dissolved by mutual
consent, and the former resolved to establish a paper of his own, in
which, upon his sole responsibility, he could advocate the doctrine of
immediate emancipation and oppose the scheme of African colonization. He
was sure, after his experiences at Baltimore, that a movement against
slavery resting upon any less radical foundation than this would be
ineffectual. He first proposed to establish his paper at Washington, in
the midst of slavery, but on returning to New England and observing the
state of public opinion there, he came to the conclusion that little
could be done at the South while the non-slaveholding North was lending
her influence, through political, commercial, religious and social
channels, for the sustenance of slavery. He determined, therefore, to
publish his paper in Boston, and, having issued his prospectus, set
himself to the task of awakening an interest in the subject by means of
lectures in some of the principal cities and towns of the North. It was
an up-hill work. Contempt for the negro and indifference to his wrongs
were almost universal. In Boston, then a great cotton mart, he tried in
vain to procure a church or vestry for the delivery of his lectures, and
thereupon announced in one of the daily journals that if some suitable
place was not promptly offered he would speak on the common. A body of
infidels under the leadership of Abner Kneeland (1774-1844), who had
previously been in turn a Baptist minister and the editor of a
Universalist magazine, proffered him the use of their small hall; and,
no other place being accessible, he accepted it gratefully, and
delivered therein (in October 1830) three lectures, in which he unfolded
his principles and plans. He visited privately many of the leading
citizens of the city, statesmen, divines and merchants, and besought
them to take the lead in a national movement against slavery; but they
all with one consent made excuse, some of them listening to his plea
with manifest impatience. He was disappointed, but not disheartened. His
conviction of the righteousness of his cause, of the evils and dangers
of slavery, and of the absolute necessity of the contemplated movement,
was intensified by opposition, and he resolved to go forward, trusting
in God for success.
On the 1st of January 1831, without a dollar of capital, and without a
single subscriber, he and his partner Isaac Knapp (1804-1843) issued the
first number of the _Liberator_, avowing their "determination to print
it as long as they could subsist on bread and water, or their hands
obtain employment." Its motto was, "Our country is the world--our
countrymen are mankind"; and the editor, in his address to the public,
uttered the words which have become memorable as embodying the whole
purpose and spirit of his life: "I am in earnest--I will not
equivocate--I will not excuse--I will not retreat a single inch--and I
will be heard." Help came but slowly. For many months Garrison and his
brave partner, who died long before the end of the conflict, made their
bed on the floor of the room, "dark, unfurnished and mean," in which
they printed their paper, and where Mayor Harrison Gray Otis of Boston,
in compliance with the request of Governor Robert Y. Hayne of South
Carolina, "ferreted them out" in "an obscure hole," "their only visible
auxiliary a negro boy." But the paper founded under such inauspicious
circumstances exerted a mighty influence, and lived to record not only
President Lincoln's proclamation of emancipation, but the adoption of an
amendment to the constitution of the United States for ever prohibiting
slavery. It was the beginning and the nucleus of an agitation that
eventually pervaded and filled every part of the country. Other
newspapers were afterwards established upon the same principles;
anti-slavery societies, founded upon the doctrine of immediate
emancipation, sprang up on every hand; the agitation was carried into
political parties, into the press, and into legislative and
ecclesiastical assemblies; until in 1861 the Southern states, taking
alarm from the election of a president known to be at heart opposed to
slavery though pledged to enforce all the constitutional safeguards of
the system, seceded from the Union and set up a separate government.
Garrison sought the abolition of slavery by moral means alone. He knew
that the national government had no power over the system in any state,
though it could abolish it at the national capital, and prohibit it in
the territories. He thought it should bring its moral influence to bear
in favour of abolition; but neither he nor his associates ever asked
Congress to exercise any unconstitutional power. His idea was to combine
the moral influence of the North, and pour it through every open channel
upon the South. To this end he made his appeal to the Northern churches
and pulpits, beseeching them to bring the power of Christianity to bear
against the slave system, and to advocate the rights of the slaves to
immediate and unconditional freedom. He was a man of peace, hating war
not less than he did slavery; but he warned his countrymen that if they
refused to abolish slavery by moral power a retributive war must sooner
or later ensue. The conflict was irrepressible. Slavery must be
overthrown, if not by peaceful means, then in blood. The first society
organized under Garrison's auspices, and in accordance with his
principles, was the New England Anti-Slavery Society, which adopted its
constitution in January 1832. In the spring of this year Garrison issued
his _Thoughts on African Colonization_, in which he showed by ample
citations from official documents that the American Colonization Society
was organized in the interest of slavery, and that in offering itself to
the people of the North as a practical remedy for that system it was
guilty of deception. His book, aided by others taking substantially the
same view, smote the society with a paralysis from which it never
recovered. Agents of the American Colonization Society in England having
succeeded in deceiving leading Abolitionists there as to its character
and tendency, Garrison was deputed by the New England Anti-Slavery
Society to visit England for the purpose of counteracting their
influence. He went in the spring of 1833, when he was but twenty-seven
years of age, and was received with great cordiality by British
Abolitionists, some of whom had heard of his bold assaults upon American
slavery, and had seen a few numbers of the _Liberator_. The struggle for
emancipation in the West Indies was then at the point of culmination;
the leaders of the cause, from all parts of the kingdom, were assembled
in London, and Garrison was at once admitted to their councils and
treated with distinguished consideration. He took home with him a
"protest" against the American Colonization Society, signed by
Wilberforce, Zachary Macaulay, Samuel Gurney, William Evans, S.
Lushington, T. Fowell Buxton, James Cropper, Daniel O'Connell and
others, in which they declared their deliberate judgment that "its
precepts were delusive," and "its real effects of the most dangerous
nature." He also received assurances of the cordial sympathy of British
Abolitionists with him in his efforts to abolish American slavery. He
gained a hearing before a large popular assembly in London, and won the
confidence of those whom he addressed by his evident earnestness,
sincerity and ability.
Garrison's visit to England enraged the pro-slavery people and press of
the United States at the outset, and when he returned home in September
with the "protest" against the Colonization Society, and announced that
he had engaged the services of George Thompson as a lecturer against
American slavery, there were fresh outbursts of rage on every hand. The
American Anti-Slavery Society was organized in December of that year
(1833), putting forth a masterly declaration of its principles and
purposes from the pen of Garrison. This added fresh fuel to the public
excitement, and when Thompson came over in the next spring, the
hostility to the cause began to manifest itself in mobs organized to
suppress the discussion of the slavery question. Now began what Harriet
Martineau called "the martyr age in America." In the autumn of 1835
Thompson was compelled, in order to save his life, to embark secretly
for England. Just before his departure the announcement that he would
address the Woman's Anti-Slavery Society of Boston created "a mob of
gentlemen of property and standing," from which, if he had been present,
he could hardly have escaped with his life. The whole city was in an
uproar. Garrison, almost denuded of his clothing, was dragged through
the streets with a rope by infuriated men. He was rescued with great
difficulty, and consigned to the gaol for safety, until he could be
secretly removed from the city.
Anti-slavery societies were greatly multiplied throughout the North, and
many men of influence, both in the church and in the state, were won to
the cause. Garrison, true to his original purpose, never faltered or
turned back. The Abolitionists of the United States were a united body
until 1839-1840, when divisions sprang up among them. Garrison
countenanced the activity of women in the cause, even to the extent of
allowing them to vote and speak in the anti-slavery societies, and
appointing them as lecturing agents; moreover, he believed in the
political equality of the sexes, to which a strong party was opposed
upon social and religious grounds. Then there were some who thought
Garrison dealt too severely with the churches and pulpits for their
complicity with slavery, and who accused him of a want of religious
orthodoxy; indeed, according to the standards of his time he was
decidedly heterodox, though he had an intensely religious nature and was
far from being an infidel, as he was often charged with being. He was,
moreover, not only a non-resistant but also an opponent of all political
systems based on force. "As to the governments of this world," he said,
"whatever their titles or forms we shall endeavour to prove that in
their essential elements, as at present administered, they are all
anti-Christ; that they can never by human wisdom be brought into
conformity with the will of God; that they cannot be maintained except
by naval and military power to carry them into effect; that all their
penal enactments, being a dead letter without any army to carry them
into effect, are virtually written in human blood; and that the
followers of Jesus should instinctively shun their stations of honor,
power, and emolument--at the same time 'submitting to every ordinance of
man for the Lord's sake' and offering no physical resistance to any of
their mandates, however unjust or tyrannical." These views were very
distasteful to many, who, moreover, felt that Garrison greatly injured
abolitionism by causing it to be associated in men's minds with these
unpopular views on other subjects. The dissentients from his opinions
determined to form an anti-slavery political party, while he believed in
working by moral rather than political party instrumentalities. These
differences led to the organization of a new National Anti-Slavery
Society in 1840, and to the formation of the "Liberty Party" (q.v.) in
politics. (See BIRNEY, JAMES G.) The two societies sent their delegates
to the World's Anti-Slavery Convention in London in 1840, and Garrison
refused to take his seat in that body, because the women delegates from
the United States were excluded. The discussions of the next few years
served to make clearer than before the practical workings of the
constitution of the United States as a shield and support of slavery;
and Garrison, after a long and painful reflection, came to the
conclusion that its pro-slavery clauses were immoral, and that it was
therefore wrong to take an oath for its support. The Southern states had
greatly enlarged representation in Congress on account of their slaves,
and the national government was constitutionally bound to assist in the
capture of fugitive slaves, and to suppress every attempt on their part
to gain their freedom by force. In view of these provisions, Garrison,
adopting a bold scriptural figure of speech, denounced the constitution
as "a covenant with death and an agreement with hell," and chose as his
motto, "No union with slaveholders."
One class of Abolitionists sought to evade the difficulty by strained
interpretations of the clauses referred to, while others, admitting that
they were immoral, felt themselves obliged, notwithstanding, to support
the constitution in order to avoid what they thought would be still
greater evils. The American Anti-Slavery Society, of which Garrison was
the president from 1843 to the day of emancipation, was during all this
period the nucleus of an intense and powerful moral agitation, which was
greatly valued by many of the most faithful workers in the field of
politics, who respected Garrison for his fidelity to his convictions. On
the other hand, he always had the highest respect for every earnest and
faithful opponent of slavery, however far their special views might
differ. When in 1861 the Southern states seceded from the Union and took
up arms against it, he saw clearly that slavery would perish in the
struggle, that the constitution would be purged of its pro-slavery
clauses, and that the Union henceforth would rest upon the sure
foundations of liberty, justice and equality to all men. He therefore
ceased from that hour to advocate disunion, and devoted himself to the
task of preparing the way for and hastening on the inevitable event. His
services at this period were recognized and honoured by President
Lincoln and others in authority, and the whole country knew that the
agitation which made the abolition of slavery feasible and necessary was
largely due to his uncompromising spirit and indomitable courage.
In 1865 at the close of the war, he declared that, slavery being
abolished, his career as an abolitionist was ended. He counselled a
dissolution of the American Anti-Slavery Society, insisting that it had
become _functus officiis_, and that whatever needed to be done for the
protection of the freedmen could best be accomplished by new
associations formed for that purpose. The _Liberator_ was discontinued
at the end of the same year, after an existence of thirty-five years. He
visited England for the second time in 1846, and again in 1867, when he
was received with distinguished honours, public as well as private. In
1877, when he was there for the last time, he declined every form of
public recognition. He died in New York on the 24th of May 1879, in the
seventy-fourth year of his age, and was buried in Boston, after a most
impressive funeral service, four days later. In 1843 a small volume of
his _Sonnets and other Poems_ was published, and in 1852 appeared a
volume of _Selections from his Writings and Speeches_. His wife, Helen
Eliza Benson, died in 1876. Four sons and one daughter survived them.
Garrison's son, WILLIAM LLOYD GARRISON (1838-1909), was a prominent
advocate of the single tax, free trade, woman's suffrage, and of the
repeal of the Chinese Exclusion Act, and an opponent of imperialism;
another son, WENDELL PHILLIPS GARRISON (1840-1907), was literary editor
of the New York _Nation_ from 1865 to 1906.
The above article, with certain modifications, reproduces the account
given in the 9th edition of this work by Oliver Johnson (reprinted
from his _Garrison: an Outline of his Life_, New York, 1879). The
writer (1809-1889) was a prominent Abolitionist, editor, and an
intimate friend of Garrison; he edited the _Liberator_ during
Garrison's absence in England in 1833, and later was an editor or an
associate editor of various journals, including, after the Civil War,
the New York _Tribune_ and the New York _Evening Post_. He also
published an excellent brief biography in _William Lloyd Garrison and
his Times_ (Boston, 1880).
The great authority on the life of Garrison is the thorough and candid
work of his sons, W.P. and F.J. Garrison, _William Lloyd Garrison
1805-1879: The Story of his Life told by his Children_ (4 vols., New
York, 1885-1889), which is indispensable for the student of the
anti-slavery struggle in America. Goldwin Smith's _The Moral Crusader:
a Biographical Essay on William Lloyd Garrison_ (New York, 1892) is a
brilliant sketch.
GARRISON, originally a term for stores or supplies, also a defence or
protection, now confined in meaning to a body of troops stationed in a
town or fortress for the purpose of defence. In form the word is derived
from O. Fr. _garison_, modern _guerison_, from _guerir_, to furnish with
stores, to preserve, but in its later meaning it has been confused with
the Fr. _garnison_, the regular word for troops stationed for purposes
of defence. In English "garnison" was used till the 16th century, when
"garrison" took its place. In the British army "garrison troops,"
especially "garrison artillery," are troops trained and employed for
garrison work as distinct from field operations.
GARROTE (Spanish for "cudgel"), an appliance used in Spain and Portugal
for the execution of criminals condemned to death. The criminal is
conducted to the place of execution (which is public) on horseback or in
a cart, wearing a black tunic, and is attended by a procession of
priests, &c. He is seated on a scaffold fastened to an upright post by
an iron collar (the garrote), and a knob worked by a screw or lever
dislocates his spinal column, or a small blade severs the spinal column
at the base of the brain. (See CAPITAL PUNISHMENT.) Originally a stout
cord or bandage was tied round the neck of the criminal, who was seated
in a chair fixed to a post. Between the cord and the neck a stick was
inserted (hence the name) and twisted till strangulation ensued.
"Garrotting" is the name given in England to a form of robbery with
violence which became rather common in the winter of 1862-1863. The
thief came up behind his victim, threw a cord over his head, and
tightened it nearly to strangulation point, while robbing him. An act of
1863, imposing the penalty of flogging in addition to penal servitude
for this offence, had the effect of stopping garrotting almost entirely.
At any rate, the practice was checked; and, though the opponents of any
sort of flogging refuse to admit that this was due to the penalty, that
view has always been taken by the English judges who had experience of
such cases.
GARRUCHA, a seaport of south-eastern Spain, in the province of Almeria;
on the Mediterranean Sea and on the right bank of the river Antas. Pop.
(1900) 4461. The harbour of Garrucha, which is defended by an ancient
castle, affords shelter to large ships, and is the natural outlet for
the commerce of a thriving agricultural and mining district. Despite its
small size and the want of railway communication, Garrucha has thus a
considerable trade in lead, silver, copper, iron, esparto grass, fruit,
&c. Besides sea-going ships, many small coasters enter in ballast, and
clear with valuable cargoes. In 1902, 135 vessels of 390,000 tons
entered the harbour, the majority being British or Spanish; and in the
same year the value of the exports reached L478,000, and that of the
imports L128,000. Both imports and exports trebled their value in the
ten years 1892-1902.
GARSTON, a seaport in the Widnes parliamentary division of Lancashire,
England, on the Mersey, 6 m. S.E. of Liverpool. Pop. (1891) 13,444;
(1901) 17,289. The docks, belonging to the London & North Western
railway company, employ most of the working population. There is about a
mile of quayage, with special machinery for the shipping of coal, which
forms the chief article of export.
GARTH, SIR SAMUEL (1661-1719), English physician and poet, was born of a
good Yorkshire family in 1661. He entered Peterhouse, Cambridge, in
1676, graduating B.A. in 1679 and M.A. in 1684. He took his M.D. and
became a member of the College of Physicians in 1691. In 1697 he
delivered the Harveian oration, in which he advocated a scheme dating
from some ten years back for providing dispensaries for the relief of
the sick poor, as a protection against the greed of the apothecaries. In
1699 he published a mock-heroic poem, _The Dispensary_, in six cantos,
which had an instant success, passing through three editions within a
year. In this he ridiculed the apothecaries and their allies among the
physicians. The poem has little interest at the present day, except as a
proof that the heroic couplet was written with smoothness and polish
before the days of Pope. Garth was a member of the Kit-Kat Club, and
became the leading physician of the Whigs, as Radcliffe was of the
Tories. In 1714 he was knighted by George I. and he died on the 18th of
January 1719. He wrote little besides his best-known work _The
Dispensary_ and _Claremont_, a moral epistle in verse. He made a Latin
oration (1700) in praise of Dryden and translated the _Life of Otho_ in
the fifth volume of Dryden's Plutarch. In 1717 he edited a translation
of Ovid's _Metamorphoses_, himself supplying the fourteenth and part of
the fifteenth book.
GARTOK, a trade-market of Tibet, situated on the bank of the Indus on
the road between Shigatse and Leh, to the east of Simla. In accordance
with the Tibet treaty of 1904, Gartok, together with Yatung and Gyantse,
was thrown open to British trade. On the return of the column from Lhasa
in that year Gartok was visited by a party under Captain Ryder, who
found only a few dozen people in winter quarters, their houses being in
the midst of a bare plain. In summer, however, all the trade between
Tibet and Ladakh passes through this place.
GARY, a city of Lake county, Indiana, U.S.A., at the southern end of
Lake Michigan, about 25 m. S.E. of Chicago, Ill. Pop. (1910 census)
16,802. Gary is served by the Baltimore & Ohio, the Lake Shore &
Michigan Southern, the Michigan Central, the Pennsylvania, the Wabash,
and (for freight only) the Chicago, Lake Shore & Eastern, and the
Indiana Harbor Belt railways, and by several steamship lines plying the
Great Lakes. There are about 21 sq. m. within the municipal limits, but
the city lies chiefly within a tract of about 8000 acres composed at the
time of its settlement mainly of sand dunes and swamps intersected from
east to west by the Grand Calumet and the Little Calumet rivers, small
streams respectively about 1 and 3 m. S. of the lake shore. In 1906 the
United States Steel Corporation bought this tract to establish on it a
great industrial community, as direct water connexion with the Lake
Superior ore region was possible, and it was comparatively accessible to
West Virginia coal and Michigan limestone, with unusual railroad
facilities. The Steel Corporation began the actual building of the town
in June 1906, the first step being the installation of an elaborate
system of sewers, and of mains and conduits, for the distribution of
water, gas and electricity. The water-supply is taken from the lake at a
point 2 m. offshore by means of a tunnel. These public utilities the
Steel Corporation controls, and it has built about 500 dwellings, two
hotels, a bank, and its own plant. A small patch of land, now within the
limits of the city, has been from the beginning in the hands of private
owners, but the remainder of the lots (except those already sold) are
owned by the Steel Corporation, and are sold under certain restrictions
intended to prevent real estate speculation, to guarantee bona fide
improvement of the property, and to restrict the sale of intoxicating
drinks. Between the Grand Calumet river (which has been dredged out into
a canal) and the lake lies the plant of the Steel Corporation, covering
about 1200 acres. All the machinery in this great plant is driven by
electricity from generators whose motive power is supplied by the
combustion of gases from the blast furnaces. From the same sources is
also supplied the electricity for lighting the city. The rail mill is
operated by three-phase induction motors of from 2000 to 6000
horse-power capacity. The city was chartered in 1906 and was named in
honour of Elbert Henry Gary (b. 1846), chairman of the board of
directors and chairman of the finance committee of the United States
Steel Corporation.
GAS, a general term for one of the three states of aggregation of
matter; also more specifically applied to coal-gas, the gaseous product
formed in the destructive distillation of coal or other carbonaceous
matter (see below, section _Gas Manufacture_; for gas engines see the
separate heading GAS ENGINE).
_The Gaseous State._--Matter is studied under three physical
phases--solids, liquids and gases, the latter two being sometimes
grouped as "fluids." The study of the physical properties of fluids in
general constitutes the science of hydromechanics, and their
applications in the arts is termed hydraulics; the special science
dealing with the physical properties of gases is named pneumatics.
The gaseous fluid with which we have chiefly to do is our atmosphere.
Though practically invisible, it appeals in its properties to other of
our senses, so that the evidences of its presence are manifold. Thus we
feel it in its motion as wind, and observe the dynamical effects of this
motion in the quiver of the leaf or the motion of a sailing ship. It
offers resistance to the passage of bodies through it, destroying their
motion and transforming their energy--as is betrayed to our hearing in
the whiz of the rifle bullet, to our sight in the flash of the meteor.
The practically obvious distinction between solids and fluids may be
stated in dynamical language thus:--solids can sustain a longitudinal
pressure without being supported by a lateral pressure; fluids cannot.
Hence any region of space enclosed by a rigid boundary can be easily
filled with a fluid, which then takes the form of the bounding surface
at every point of it. But here we distinguish between fluids according
as they are gases or liquids. The gas will always completely fill the
region, however small the quantity put in. Remove any portion and the
remainder will expand so as to fill the whole space again. On the other
hand, it requires a definite quantity of liquid to fill the region.
Remove any portion and a part of the space will be left unoccupied by
liquid. Part of the liquid surface is then otherwise conditioned than by
the form of the wall or bounding surface of the region; and if the
portion of the wall not in contact with the liquid is removed the form
and quantity of the liquid are in no way affected. Hence a liquid can be
kept in an open vessel; a gas cannot so be. To quote the differentia of
Sir Oliver Lodge: "A solid has volume and shape; a liquid has volume,
but no shape; a gas has neither volume nor shape."
It is necessary to distinguish between a gas and a "vapour." The latter
possesses the physical property stated above which distinguishes a gas
from a fluid, but it differs from a gas by being readily condensible to
a liquid, either by lowering the temperature or moderately increasing
the pressure. The study of the effects of pressure and temperature on
many gases led to the introduction of the term "permanent gases" to
denote gases which were apparently not liquefiable. The list included
hydrogen, nitrogen and oxygen; but with improved methods these gases
have been liquefied and even solidified, thus rendering the term
meaningless (see LIQUID GASES). The term "perfect gas" is applied to an
imaginary substance in which there is no frictional retardation of
molecular motion; or, in other words, the time during which any molecule
is influenced by other molecules is infinitesimally small compared with
the time during which it traverses its mean free path. It serves as a
means of research, more particularly in mathematical investigations, the
simple laws thus deduced being subsequently modified by introducing
assumptions in order to co-ordinate actual experiences.
The gaseous state was well known to the ancients; for instance, in Greek
cosmology, "air" ([Greek: pneuma]) was one of the fundamental elements.
The alchemists used such terms as _spiritus_, _flatus_, _halitus_,
_aura_, _emanatio nubila_, &c., words implying a "wind" or "breath." The
word "gas" was invented by J.B. van Helmont in his _Ortus medicinae_,
posthumously published in 1648, in the course of his description of the
gas now known as carbon dioxide. He found that charcoal on burning
yielded a "spirit," which he named _spiritus sylvestris_ on account of
its supposed untamable nature ("Gas sylvestre sive incoercibile, quod in
corpus cogi non potest visibile"); and he invented the word "gas" in the
expression: "... this spirit, hitherto unknown, ... I call by a new name
_gas_" ("hunc spiritum, incognitum hactenus, novo nomine _gas_ voco").
The word was suggested by the Gr. [Greek: chaos], chaos, for he also
writes: "I have called this spirit _gas_, it being scarcely
distinguishable from the Chaos of the ancients" ("halitum illum _Gas_
vocavi, non longe a Chao veterum secretum"). The view that the word was
suggested by the Dutch _geest_, spirit, is consequently erroneous. Until
the end of the 18th century the word "air," qualified by certain
adjectives, was in common use for most of the gases known--a custom due
in considerable measure to the important part which common air played in
chemical and physical investigations.
The study of gases may be divided into two main branches: the physical
and the chemical. The former investigates essentially general
properties, such as the weight and density, the relation between
pressure, volume and temperature (piezometric and thermometric
properties), calorimetric properties, diffusion, viscosity, electrical
and thermal conductivity, &c., and generally properties independent of
composition. These subjects are discussed in the articles DENSITY;
THERMOMETRY; CALORIMETRY; DIFFUSION; CONDUCTION OF HEAT; and
CONDENSATION OF GASES. The latter has for its province the preparation,
collection and identification of gases, and the volume relations in
which they combine; in general it deals with specific properties. The
historical development of the chemistry of gases--pneumatic
chemistry--is treated in the article CHEMISTRY; the technical analysis
of gaseous mixtures is treated below under _Gas Analysis_. Connecting
the experimental study of the physical and chemical properties is the
immense theoretical edifice termed the kinetic theory of gases. This
subject, which is discussed in the article MOLECULE, has for its purpose
(1) the derivation of a physical structure of a gas which will agree
with the experimental observations of the diverse physical properties,
and (2) a correlation of the physical properties and chemical
composition.
_Gas Analysis._--The term "gas analysis" is given to that branch of
analytical chemistry which has for its object the quantitative
determination of the components of a gaseous mixture. The chief
applications are found in the analysis of flue gases (in which much
information is gained as to the completeness and efficiency of
combustion), and of coal gas (where it is necessary to have a product of
a definite composition within certain limits). There are, in addition,
many other branches of chemical technology in which the methods are
employed. In general, volumetric methods are used, i.e. a component is
absorbed by a suitable reagent and the diminution in volume noted, or it
is absorbed in water and the amount determined by titration with a
standard solution. Exact analysis is difficult and tedious, and
consequently the laboratory methods are not employed in technology,
where time is an important factor and moderate accuracy is all that is
necessary. In this article an outline of the technical practice will be
given.
The apparatus consists of (1) a measuring vessel, and (2) a series of
absorption pipettes. A convenient form of measuring vessel is that
devised by W. Hempel. It consists of two vertical tubes provided with
feet and connected at the bottom by flexible rubber tubing. One tube,
called the "measuring tube," is provided with a capillary stopcock at
the top and graduated downwards; the other tube, called the "level
tube," is plain and open. To use the apparatus, the measuring tube is
completely filled with water by pouring water into both tubes, raising
the level tube until water overflows at the stopcock, which is then
turned. The test gas is brought to the stopcock, by means of a fine tube
which has been previously filled with water or in which the air has been
displaced by running the gas through. By opening the stopcock and
lowering the level tube any desired quantity of the gas can be aspirated
over. In cases where a large quantity of gas, i.e. sufficient for
several tests, is to be collected, the measuring tube is replaced by a
large bottle.
[Illustration: (By permission of Messrs Baird & Tatlock.)
FIG. 1.
FIG. 2.]
The volume of the gas in the measuring tube is determined by bringing
the water in both tubes to the same level, and reading the graduation on
the tube, avoiding parallax and the other errors associated with
recording the coincidence of a graduation with a meniscus. The
temperature and atmospheric pressure are simultaneously noted. If the
tests be carried out rapidly, the temperature and pressure may be
assumed to be constant, and any diminution in volume due to the
absorption of a constituent may be readily expressed as a percentage.
If, however, the temperature and pressure vary, the volumes are reduced
to 0 deg. and 760 mm. by means of the formula V0 = V(P-p)/(1 +
.00366t)760, in which V is the observed volume, P the barometric
pressure, p the vapour tension of water at the temperature t of the
experiment. This reduction is facilitated by the use of tables.
Some common forms of absorption pipettes are shown in figs. 1 and 2. The
simpler form consists of two bulbs connected at the bottom by a wide
tube. The lower bulb is provided with a smaller bulb bearing a capillary
through which the gas is led to the apparatus, the higher bulb has a
wider outlet tube. The arrangement is mounted vertically on a stand.
Sometimes the small bulb on the left is omitted. The form of the pipette
varies with the nature of the absorbing material. For solutions which
remain permanent in air the two-bulbed form suffices; in other cases a
composite pipette (fig. 2) is employed, in which the absorbent is
protected by a second pipette containing water. In the case of solid
reagents, e.g. phosphorus, the absorbing bulb has a tubulure at the
bottom. To use a pipette, the absorbing liquid is brought to the outlet
of the capillary by tilting or by squeezing a rubber ball fixed to the
wide end, and the liquid is maintained there by closing with a clip. The
capillary is connected with the measuring tube by a fine tube previously
filled with water. The clip is removed, the stopcock opened, and the
level tube of the measuring apparatus raised, so that the gas passes
into the first bulb. There it is allowed to remain, the pipette being
shaken from time to time. It is then run back into the measuring tube by
lowering the level tube, the stopcock is closed, and the volume noted.
The operation is repeated until there is no further absorption.
The choice of absorbents and the order in which the gases are to be
estimated is strictly limited. Confining ourselves to cases where
titration methods are not employed, the general order is as follows:
carbon dioxide, olefines, oxygen, carbon monoxide, hydrogen, methane and
nitrogen (by difference). This scheme is particularly applicable to
coal-gas. Carbon dioxide is absorbed by a potash solution containing one
part of potash to between two and three of water; the stronger solution
absorbs about 40 volumes of the gas. The olefines--ethylene, &c.--are
generally absorbed by a very strong sulphuric acid prepared by adding
sulphur trioxide to sulphuric acid to form a mixture which solidifies
when slightly cooled. Bromine water is also employed. Oxygen is absorbed
by stick phosphorus contained in a tubulated pipette filled with water.
The temperature must be above 18 deg.; and the absorption is prevented by
ammonia, olefines, alcohol, and some other substances. An alkaline
solution of pyrogallol is also used; this solution rapidly absorbs
oxygen, becoming black in colour, and it is necessary to prepare the
solution immediately before use. Carbon monoxide is absorbed by a
solution of cuprous chloride in hydrochloric acid or, better, in
ammonia. When small in amount, it is better to estimate as carbon
dioxide by burning with oxygen and absorbing in potash; when large in
amount, the bulk is absorbed in ammoniacal cuprous chloride and the
residue burned. Hydrogen may be estimated by absorption by heated
palladium contained in a capillary through which the gas is passed, or
by exploding (under reduced pressure) with an excess of oxygen, and
measuring the diminution in volume, two-thirds of which is the volume of
hydrogen. The explosion method is unsatisfactory when the gas is
contained over water, and is improved by using mercury. Methane cannot
be burnt in this way even when there is much hydrogen present, and
several other methods have been proposed, such as mixing with air and
aspirating over copper oxide heated to redness, or mixing with oxygen
and burning in a platinum tube heated to redness, the carbon dioxide
formed being estimated by absorption in potash. Gases soluble in water,
such as ammonia, hydrochloric acid, sulphuretted hydrogen, sulphur
dioxide, &c., are estimated by passing a known volume of the gas through
water and titrating the solution with a standard solution. Many types of
absorption vessel are in use, and the standard solutions are generally
such that 1 c.c. of the solution corresponds to 1 c.c. of the gas under
normal conditions.
[Illustration: (By permission of Messrs Baird & Tatlock.)
FIG. 3.]
Many forms of composite gas-apparatus are in use. One of the commonest
is the Orsat shown in fig. 3. The gas is measured in the graduated
cylinder on the right, which is surrounded by a water jacket and
provided with a levelling bottle. At the top it is connected by a
capillary tube bent at right angles to a series of absorbing vessels,
the connexion being effected by stopcocks. These vessels consist of two
vertical cylinders joined at the bottom by a short tube. The cylinder in
direct communication with the capillary is filled with glass tubes so as
to expose a larger surface of the absorbing solution to the gas. The
other cylinder is open to the air and serves to hold the liquid ejected
from the absorbing cylinder. Any number of bulbs can be attached to the
horizontal capillary; in the form illustrated there are four, the last
being a hydrogen pipette in which the palladium is heated in a
horizontal tube by a spirit lamp. At the end of the horizontal tube
there is a three-way cock connecting with the air or an aspirator. To
use the apparatus, the measuring tube is completely filled with water by
raising the levelling bottle. The absorbing vessels are then about half
filled with the absorbents, and, by opening the cocks and aspirating,
the liquid is brought so as completely to fill the bulbs nearer the
capillary. The cocks are then closed. By opening the three-way cock to
the supply of the test gas and lowering the levelling bottle, any
desired amount can be drawn into the measuring tube. The absorption is
effected by opening the cock of an absorbing vessel and raising the
levelling bottle. The same order of absorption and general directions
pertaining to the use of Hempel pipettes have to be adopted.
Although the earliest attempts at gas analysis were made by Scheele,
Priestley, Cavendish, Lavoisier, Dalton, Gay-Lussac and others, the
methods were first systematized by R. Bunsen, who began his researches
in 1838. He embodied his results in his classical _Gasometrische
Methoden_ (1857, second edition 1877), a work translated into English
by H. Roscoe. Clemens Winkler contributed two works, _Anleitung zur
chemischen Untersuchung der Industriegase_ (1876-1877) and _Lehrbuch
der technischen Gasanalyse_ (2nd ed., 1892), both of which are very
valuable for the commercial applications of the methods. W. Hempel's
researches are given in his _Neue Methode zur Analyse der Gase_ (1880)
and _Gasanalytische Methoden_ (1890, 3rd ed. 1900).
GAS MANUFACTURE
Historical.
1. _Illuminating Gas._--The first practical application of gas distilled
from coal as an illuminating agent is generally ascribed to William
Murdoch, who between the years of 1792 and 1802 demonstrated the
possibility of making gas from coal and using it as a lighting agent on
a large scale. Prior to 1691, however, Dr John Clayton, dean of Kildare,
filled bladders with inflammable gas obtained by the distillation of
coal, and showed that on pricking the bladders and applying a light to
the escaping gas it burnt with a luminous flame, and in 1726 Stephen
Hales published the fact that by the distillation of 158 grains of
Newcastle coal, 180 cub. in. of inflammable air would be obtained. Jean
Pierre Minckelers, professor of natural philosophy in the university of
Louvain, and later of chemistry and physics at Maestricht, made
experiments on distilling gas from coal with the view of obtaining a
permanent gas sufficiently light for filling balloons, and in 1785
experimentally lighted his lecture room with gas so obtained as a
demonstration to his students, but no commercial application was made of
the fact. Lord Dundonald, in 1787, whilst distilling coal for the
production of tar and oil, noticed the formation of inflammable gas, and
even used it for lighting the hall of Culross Abbey. It is clear from
these facts that, prior to Murdoch's experiments, it was known that
illuminating gas could be obtained by the destructive distillation of
coal, but the experiments which he began at Redruth in 1792, and which
culminated in the lighting of Messrs Boulton, Watt & Co.'s engine works
at Soho, near Birmingham, in 1802, undoubtedly demonstrated the
practical possibility of making the gas on a large scale, and burning it
in such a way as to make coal-gas the most important of the artificial
illuminants. An impression exists in Cornwall, where Murdoch's early
experiments were made, that it was a millwright named Hornblower who
first suggested the process of making gas to Murdoch, but, as has been
shown, the fact that illuminating gas could be obtained from coal by
distillation was known a century before Murdoch made his experiments,
and the most that can be claimed for him is that he made the first
successful application of it on a practical scale.
In 1799 a Frenchman named Philippe Lebon took out a patent in Paris for
making an illuminating gas from wood, and gave an exhibition of it in
1802, which excited a considerable amount of attention on the European
continent. It was seen by a German, F.A. Winsor, who made Lebon an offer
for his secret process for Germany. This offer was, however, declined,
and Winsor returned to Frankfort determined to find out how the gas
could be made. Having quickly succeeded in discovering this, he in 1803
exhibited before the reigning duke of Brunswick a series of experiments
with lighting gas made from wood and from coal. Looking upon London as a
promising field for enterprise, he came over to England, and at the
commencement of 1804 took the Lyceum theatre, where he gave
demonstrations of his process. He then proceeded to float a company,
and in 1807 the first public street gas lighting took place in Pall
Mall, whilst in 1809 he applied to parliament to incorporate the
National Heat and Light Company with a capital of half a million
sterling. This application was opposed by Murdoch on the ground of his
priority in invention, and the bill was thrown out, but coming to
parliament for a second time in 1810, Winsor succeeded in getting it
passed in a very much curtailed form, and, a charter being granted later
in 1812, the company was called the Chartered Gas Light and Coke
Company, and was the direct forerunner of the present London Gas Light
and Coke Company. During this period Frederick C. Accum (1769-1838), Dr
W. Henry and S. Clegg did so much by their writings and by the
improvements they introduced in the manufacture, distribution and
burning of coal gas, that their names have become inseparably connected
with the subject.
The growth of gas lighting.
In 1813 Westminster Bridge, and in the following year the streets of
Westminster, were lighted with gas, and in 1816 it became common in
London. After this so rapid was the progress of this new mode of
illumination that in the course of a few years it was adopted by all the
principal towns in the United Kingdom for lighting streets as well as
shops and public edifices. In private houses it found its way more
slowly, partly from an apprehension of danger attending its use, and
partly from the discomfort which was experienced in many cases through
the gas being distributed without purification, and to the careless and
imperfect manner in which the service pipes were first fitted. It was
during the last four decades of the 19th century that the greatest
advance was made, this period having been marked not only by many
improvements in the manufacture of illuminating gas, but by a complete
revolution in the methods of utilizing it for the production of light.
In 1875 the London Argand, giving a duty of 3.2 candles illuminating
power per cubic foot of ordinary 16 candle gas, was looked upon as the
most perfect burner of the day, and little hope was entertained that any
burner capable of universal adoption would surpass it in its power of
developing light from the combustion of coal gas; but the close of the
century found the incandescent mantle and the atmospheric burner
yielding six times the light that was given by the Argand for the
consumption of an equal volume of gas, and to-day, by supplying gas at
an increased pressure, a light of ten times the power may be obtained.
Since the advent of the incandescent mantle, the efficiency of which is
dependent upon the heating power of the gas more than on its
illuminating power, the manufacture of coal gas has undergone
considerable modifications.
Coals used for gas-making.
Coal, the raw material from which the gas is produced by a process of
destructive distillation, varies very widely in composition (see
COAL), and it is only the class of coals rich in hydrogen, known as
bituminous coal, that can with advantage be utilized in gas
manufacture. Coals of this character are obtained in England from the
Newcastle and Durham field, South Yorkshire, Derbyshire and Barnsley
districts, and an idea of their ultimate composition may be derived
from the following table:--
+--------------------------+-------+------+--------+------+-------+------+------+
| |Carbon.|Hydro-|Sulphur.|Nitro-|Oxygen.| Ash. |Moist-|
| | | gen. | | gen. | | | ure. |
+--------------------------+-------+------+--------+------+-------+------+------+
| Newcastle gas coal | 82.16 | 4.83 | 1.00 | 1.23 | 6.82 | 3.20 | 0.76 |
| Durham gas coal | 84.34 | 5.30 | 0.73 | 1.73 | 4.29 | 2.42 | 1.14 |
| South Yorkshire silkstone| 80.46 | 5.09 | 1.66 | 1.67 | 6.79 | 3.30 | 1.03 |
| Derbyshire silkstone | 76.96 | 5.04 | 2.39 | 1.77 | 6.92 | 3.28 | 3.64 |
| Barnsley gas coal | 75.64 | 4.94 | 2.84 | 1.65 | 7.25 | 4.28 | 3.40 |
+--------------------------+-------+------+--------+------+-------+------+------+
Our knowledge of the composition of coal is limited to the total
amount of carbon, hydrogen, nitrogen, oxygen and foreign materials
which it contains; and at present we know practically but little of
the way in which these bodies are combined. This being so, the
ordinary analysis of a coal affords but little indication of its value
for gas-making purposes, which can only be really satisfactorily
arrived at by extended use on a practical scale. Bituminous coal,
however, may be looked upon as containing carbon and also simple
hydrocarbons, such as some of the higher members of the paraffin
series, and likewise organic bodies containing carbon, hydrogen,
nitrogen, oxygen and sulphur.
Destructive distillation of coal.
On submitting a complex substance of this character to destructive
distillation, it will be found that the yield and quality of the
products will vary very considerably with the temperature existing in
the retorts, with the size of the charge of coal used, with its
distribution in the retort, with the length of time the distillation
has been going on, and with an infinity of other factors of a more or
less complex nature. If bituminous coal is distilled at a low
temperature, the tar is found to contain considerable quantities of
light paraffin oils; and there is no doubt that paraffin hydrocarbons
are present in the original coal. These paraffins, under the influence
of heat, split up into simpler members of the same series and into
olefines; and if we imagine the action in its simplest form, we should
have the gases, as they were evolved, consisting of (say) ethane and
ethylene. These have now to pass down the heated retort on their way
to the ascension pipe, and the contact with the heated sides of the
retort, and the baking from the radiant heat in the retort, set up an
infinity of changes. Ethane, when heated to this degree, splits up
into ethylene and hydrogen, whilst ethylene decomposes to methane and
acetylene, and the acetylene at once polymerizes to benzene,
styrolene, retene, &c. A portion also condenses, and at the same time
loses some hydrogen, becoming naphthalene; and the compounds so formed
by interactions amongst themselves build up the remainder of the
hydrocarbons present in the coal tar, whilst the organic substances
containing oxygen in the coal break down, and cause the formation of
the phenols in the tar.
There is very little doubt that the general course of the
decompositions follows these lines; but any such simple explanation of
the actions taking place is rendered impossible by the fact that,
instead of the breaking-down of the hydrocarbons being completed in
the coal, and only secondary reactions taking place in the retort, in
practice the hydrocarbons to a great extent leave the coal as the
vapours of condensible hydrocarbons, and the breaking down of these to
such simple gaseous compounds as ethylene is proceeding in the retort
at the same time as the breaking up of the ethylene already formed
into acetylene and methane, and the polymerization of the former into
higher compounds. Starting with a solid hydrocarbon of definite
composition, it would be theoretically possible to decompose it
entirely into carbon, hydrogen, ethylene and methane, and, by rapidly
removing these from the heating zone before any secondary actions took
place, to prevent formation of tar. But any such ideal is hopeless in
practice, as the coal is not a definite compound, and it is impossible
to subject it to a fixed temperature.
Effect of temperature in the retort.
If the retorts are at a temperature of 1000 deg. C. when the charge of
coal is put in, the temperature of the distillation will vary from
about 800 deg. C. close to the walls, to about 400 deg. C. in the
centre of the coal; and in the same way, in the space above the coal,
the products which come in contact with the sides of the retort are
heated to 1000 deg. C., whilst the gas near the coal is probably
heated to only 600 deg. C. Moreover, the gases and vapours in the
retort are subjected to a period of heating which varies widely with
the distance from the mouth of the retort of the coal that is
undergoing carbonization. The gas developed by the coal near the mouth
of the retort is quickly washed out into the ascension pipe by the
push of the gas behind, and the period for which it has been exposed
to the radiant heat from the walls of the retort is practically nil;
whilst the gas evolved in the portion of the retort farthest from the
mouthpiece has only its own rate of evolution to drive it forward, and
has to traverse the longest run possible in the retort, exposed during
the whole of that period to radiant heat and to contact with the
highly heated surface of the retort itself. Hence we find that the tar
is formed of two distinct sets of products, the first due to
incomplete decomposition and the second to secondary reactions due to
the products of the decomposition being kept too long in the zone of
heat.
Of the first class, the light paraffin oils and pitch may be taken as
examples; whilst benzene, naphthalene and retort carbon represent the
second. The formation of the second class of bodies is a great loss to
the gas manufacturer, as, with the exception of the trace of benzene
carried with the gas as vapour, these products are not only useless in
the gas, but one of them, naphthalene, is a serious trouble, because
any trace carried forward by the gas condenses with sudden changes of
temperature, and causes obstructions in the service pipes, whilst
their presence in the tar means the loss of a very large proportion of
the illuminating constituents of the gas. Moreover, these secondary
products cannot be successfully reduced, by further heating, to
simpler hydrocarbons of any high illuminating value, and such bodies
as naphthalene and anthracene have so great a stability that, when
once formed, they resist any efforts again to decompose them by heat,
short of the temperature which breaks them up into methane, carbon and
hydrogen.
The ammonia is derived from the nitrogen present in the coal combining
with hydrogen during destructive distillation, the nitrogen becoming
distributed amongst all three classes of products. The following table
will give an approximate idea of the proportions which go to each:--
Per cent.
Nitrogen as ammonia 14.50
" as cyanogen 1.56
" free in gas and combined in tar 35.26
" remaining in coke 48.68
------
100.00
The effect produced by alteration in the temperature of the retort
upon the composition of both gas and tar is very marked. As the
temperature is raised, the yield of gas from a given weight of coal
increases; but with the increase of volume there is a marked decrease
in the illuminating value of the gas evolved. Lewis T. Wright found,
in a series of experiments, that, when four portions of the same coal
were distilled at temperatures ranging from a dull red heat to the
highest temperature attainable in an iron retort, he obtained the
following results as to yield and illuminating power:--
+-----------------+-------------+------------+---------+
| | Cubic ft. of|Illuminating| Total |
| Temperature. | Gas per ton.| Power, | Candles |
| | | Candles. | per ton.|
+-----------------+-------------+------------+---------+
| 1. Dull red | 8,250 | 20.5 | 33.950 |
| 2. Hotter | 9,693 | 17.8 | 34.510 |
| 3. " | 10,821 | 16.7 | 36.140 |
| 4. Bright orange| 12,006 | 15.6 | 37.460 |
+-----------------+-------------+------------+---------+
_Composition of the Gas._
+-----------------+-----------+-----------+-----------+
| | 1. | 2. | 4. |
| | Per cent. | Per cent. | Per cent. |
+-----------------+-----------+-----------+-----------+
| Hydrogen | 38.09 | 43.77 | 48.02 |
| Marsh gas | 42.72 | 34.50 | 30.70 |
| Olefines | 7.55 | 5.83 | 4.51 |
| Carbon monoxide | 8.72 | 12.50 | 13.96 |
| Nitrogen | 2.92 | 3.40 | 2.81 |
| +-----------+-----------+-----------+
| | 100.00 | 100.00 | 100.00 |
+-----------------+-----------+-----------+-----------+
The gas analysis of No. 3 was lost, but the illuminating power shows
that it was intermediate in composition between Nos. 2 and 4. From
this it will be seen that, with the increase of temperature, the
hydrocarbons--the olefines and marsh gas series--gradually break up,
depositing carbon in the crown of the retort, and liberating hydrogen,
the percentage of which steadily increases with the rise of
temperature.
The tar formed is affected to an even greater extent than the gas by
alterations in the temperature at which the destructive distillation
takes place. The lower the temperature, the smaller will be the volume
of gas produced, and the lighter the specific gravity of the tar,
whilst with increase of temperature, the volume of gas rapidly rises,
and so does the specific gravity of the tar. Working with a caking
coal Wright obtained the following results:--
+--------------+------------------+
| Yield of Gas | Specific Gravity |
| per ton, | of Tar. |
| Cub. ft. | |
+--------------+------------------+
| 6,600 | 1.086 |
| 7,200 | 1.120 |
| 8,900 | 1.140 |
| 10,162 | 1.154 |
| 11,700 | 1.206 |
+--------------+------------------+
Analysis of the tar showed that the increase of the specific gravity
was due to the increase in the quantity of pitch, which rose from
28.89 to 64.08% in the residuals; whilst the ammonia, naphtha and
light oils steadily fell in quantity, the creosote and anthracene oils
doing the same, but to a smaller extent. Naphthalene also begins to
show in quantity in the tar as soon as the yield of gas reaches 10,000
cub. ft. per ton of coal carbonized.
In spite of these variations, however, the products in their main
characteristics will remain the same. They may be divided into--(a)
Solids, such as the coke and retort carbon; (b) liquids, consisting of
the tar and ammoniacal liquor; and (c) gases, consisting of the
unpurified coal gas. The proportions in which the products are
approximately obtained from a ton of gas coal have been given as
follows:--
10,000 cub. ft. of gas = 380 lb. = 17.0 per cent.
10 gallons of tar = 115 " = 5.1 "
Gas liquor[1] = 177 " = 7.9 "
Coke = 1568 " = 70.0 "
---- -----
2240 100.0
Solid products.
The chief solid residue, coke, is not absolutely pure carbon, as it
contains the mineral non-volatile constituents which remain behind as
ash when the original coal is burnt, and which, to a great extent,
existed in the sap that filled the cells of the plant from which the
coal was formed. The retort carbon formed as a dense deposit on the
crown of the retort by the action of the high temperature on the
hydrocarbons is, however, carbon in a very pure form, and, on account
of its density, is largely used for electrical purposes.
Liquid products.
The liquid products of the destructive distillation of coal are tar
and ammoniacal liquor. Tar derived from ordinary bituminous coal is a
black, somewhat viscid liquid, varying in specific gravity from 1.1 to
1.2. The ultimate composition of tar made in the London Gas Works is
approximately as follows:--
Carbon 77.53
Hydrogen 6.33
Nitrogen 1.03
Sulphur 0.61
Oxygen 14.50
------
100.00
These elements in tar are built up into an enormous number of
compounds (see COAL TAR), and its value as a by-product may be
gathered from the fact that on fractional distillation it yields--(1)
benzene and its homologues, from which aniline, the source of most of
the coal-tar colours, can be derived; (2) carbolic acid, from which
picric acid, used as a dye, a powerful explosive, and to give the
bitter flavour to some kinds of beer, is made, also many most valuable
disinfectants; (3) naphthalene, used for disinfecting, and also as the
"Albo-carbon" employed in an enriching burner for gas; (4) pitch,
extensively used in path-making, from which such bodies as anthracene
and saccharin can be extracted.
The second liquid product of the destructive distillation of coal is
the ammoniacal or gas liquor, which consists of water containing
ammonia salts in solution, partly condensed from the hot gas, and
partly added to wash the gas in the scrubbers. It contains, as its
principal constituents, ammonia, partly combined with carbonic acid
and sulphuretted hydrogen to form compounds which are decomposed on
boiling, with evolution of ammonia gas, and partly combined with
stronger acids to form compounds which require to be acted upon by a
strong alkali before the ammonia contained in them can be liberated.
The ammonia in the first class of compounds is technically spoken of
as "free"; that present in the latter as "fixed." The following
analysis by L.T. Wright will give an idea of the relative quantities
in which these compounds exist in the liquor:--
Grammes per litre.
/ Ammonium sulphide 3.03
Free < Ammonium carbonate 39.16
\ Ammonium chloride 14.23
/ Ammonium thiocyanate 1.80
Fixed < Ammonium sulphate 0.19
| Ammonium thiosulphate 2.80
\ Ammonium ferrocyanide 0.41
From a scientific point of view, the term "free" is absolutely
incorrect, and in using it the fact must be clearly borne in mind that
in this case it merely stands for ammonia, which can be liberated on
simply boiling the liquor.
Gaseous products.
The gas which is obtained by the destructive distillation of coal, and
which we employ as our chief illuminant, is not a definite compound,
but a mechanical mixture of several gases, some of which are reduced
to the lowest limit, in order to develop as fully as possible the
light-giving properties of the most important constituents of the gas.
The following analysis gives a fair idea of the composition of an
average sample of gas made from coal, purified but without
enrichment:--
Hydrogen 52.22
Unsaturated hydrocarbons 3.47
Saturated hydrocarbons 34.76
Carbon monoxide 4.23
Carbon dioxide 0.60
Nitrogen 4.23
Oxygen 0.49
------
100.00
These constituents may be divided into--(a) light-yielding
hydrocarbons, (b) combustible diluents and (c) impurities. The
hydrocarbons, upon which the luminosity of the flame entirely depends,
are divided in the analysis into two groups, saturated and
unsaturated, according to their behaviour with a solution of bromine
in potassium bromide, which has the power of absorbing those termed
"unsaturated," but does not affect in diffused daylight the gaseous
members of the "saturated" series of hydrocarbons. They may be
separated in a similar way by concentrated sulphuric acid, which has
the same absorbent effect on the one class, and not on the other. The
chief unsaturated hydrocarbons present in coal gas are: ethylene,
C2H4, butylene, C4H8, acetylene, C2H2, benzene, C6H6, and naphthalene,
C10H8, and the saturated hydrocarbons consist chiefly of methane, CH4,
and ethane, C2H6.
The light-giving power of coal gas is undoubtedly entirely due to the
hydrocarbons. The idea held up to about 1890 was that the illuminating
value depended upon the amount of ethylene present. This, however, is
manifestly incorrect, as, if it were true, 4% of ethylene mixed with
96% of a combustible diluent such as hydrogen should give 16- to
17-candle gas, whereas a mixture of 10% of ethylene and 90% of
hydrogen is devoid of luminosity. In 1876 M.P.E. Berthelot came to
the conclusion that the illuminating value of the Paris coal gas was
almost entirely due to benzene vapour. But here again another mistaken
idea arose, owing to a faulty method of estimating the benzene, and
there is no doubt that methane is one of the most important of the
hydrocarbons present, when the gas is burnt in such a way as to evolve
from it the proper illuminating power, whilst the benzene vapour,
small as the quantity is, comes next in importance and the ethylene
last. It is the combined action of the hydrocarbons which gives the
effect, not any one of them acting alone.
The series of operations connected with the manufacture and
distribution of coal gas embraces the processes of distillation,
condensation, exhaustion, wet purification by washing and scrubbing,
dry purification, measuring, storing and distribution to the mains
whence the consumer's supply is drawn.
[Illustration: FIG. 4.--Plan of Works.]
Site of gas works.
The choice of a site for a gas works is necessarily governed by local
circumstances; but it is a necessity that there should be a ready
means of transport available, and for this reason the works should be
built upon the banks of a navigable river or canal, and should have a
convenient railway siding. By this means coal may be delivered direct
to the store or retort-house, and in the same way residual products
may be removed. The fact that considerable area is required and that
the works do not improve the neighbourhood are important conditions,
and although economy of space should be considered, arrangements
should be such as to allow of extension. In the case of a works whose
daily make of gas exceeds four to five million cub. ft., it is usual
to divide the works into units, there being an efficiency limit to the
size of apparatus employed. Under these conditions the gas is dealt
with in separate streams, which mix when the holder is reached. From
the accompanying ground plan of a works (fig. 4) it will be possible
to gain an idea of the order in which the operations in gas
manufacture are carried out and the arrangement of the plant.
[Illustration: FIG. 5.--Cross Section of Retorts.]
Retorts.
The retorts in which the coal is carbonized are almost universally
made of fire-clay, and in all but small country works the old
single-ended retort, which was about 9 ft. in length, has given way to
a more economical construction known as doubles, double-ended, or
"through" retorts. These are from 18 to 22 ft. long, and as it is
found inconvenient to produce this length in one piece, they are
manufactured in three sections, the jointing together of which demands
great care. The two outer pieces are swelled at one end to take an
iron mouthpiece. The cross sections generally employed for retorts are
known as "D-shaped," "oval" and "round" (fig. 5). The "D" form is
mostly adopted owing to its power of retaining its shape after long
exposure to heat, and the large amount of heating surface it presents
at its base. The life of this retort is about thirty working months. A
cast iron mouthpiece and lid is bolted to the exterior end of each
retort, the mouthpiece carrying a socket end to receive the ascension
pipe, through which the gas passes on leaving the retort. The retorts
are heated externally and are set in an arch, the construction
depending upon the number of retorts, which varies from three to
twelve. The arch and its retorts is termed a bed or setting, and a row
of beds constitutes a bench. It is usual to have a separate furnace
for each setting, the retorts resting upon walls built transversely in
the furnace.
The heating of the retorts is carried out either by the "direct
firing" or by the "regenerative" system, the latter affording marked
advantages over the former method, which is now becoming extinct. In
the regenerative system of firing, a mixture of carbon monoxide and
nitrogen is produced by passing air through incandescent gas coke in a
generator placed below the bench of retorts, and the heating value of
the gases so produced is increased in most cases by the admixture of a
small proportion of steam with the primary air supply, the steam being
decomposed by contact with the red-hot coke in the generator into
water gas, a mixture of carbon monoxide and hydrogen (see FUEL:
_Gaseous_). The gases so formed vary in proportion with the
temperature of the generator and the amount of steam, but generally
contain 32 to 38% of combustible gas, the remainder being the residual
nitrogen of the air and carbon dioxide. These gases enter the
combustion chamber around the retorts at a high temperature, and are
there supplied with sufficient air to complete their combustion, this
secondary air supply being heated by the hot products of combustion on
their way to the exit flue. This method of firing results in the
saving of about one-third the weight of coke used in the old form of
furnace per ton of coal carbonized, and enables higher temperatures to
be obtained, the heat being also more equally distributed.
[Illustration: FIG. 6.--Regenerative Setting.]
There are a great number of methods of applying the regenerative
principle which vary only in detail. Fig. 6 gives an idea of the
general arrangement. The furnace A is built of fire-brick, coke is
charged at the top through the iron door B, and near the bottom are
placed fire bars C, upon which the fuel lies. The primary air
necessary for the partial combustion of the coke to "producer" gas
enters between these bars. The gases are conducted from the furnace to
the combustion chamber E through the nostrils D D, and the secondary
air is admitted at the inlet F a little above, this air having been
already heated by traversing the setting. Complete combustion takes
place at this point with the production of intense heat, the gases on
rising are baffled in order to circulate them in every direction round
the retorts, and upon arriving at the top of the setting they are
conducted down a hollow chamber communicating with the main flue and
shaft. The amount of draft which is necessary to carry out the
circulation of the gases and to draw in the adequate amount of air is
regulated by dampers placed in the main flue. By analysis of the
"producer" and "spent" gases this amount can be readily gauged.
Retorts are set in either the horizontal, inclined or vertical
position, and the advantages of the one over the other is a question
upon which almost every gas engineer has his own views.
Charging and drawing.
The introduction of labour-saving appliances into gas works has
rendered the difficult work of charging and discharging horizontal
retorts comparatively simple. Formerly it was the practice to carry
out such operations entirely by hand, men charging the retorts either
by means of shovel or hand-scoop, and the coke produced being
withdrawn with hand rakes. Now, however, only the smaller gas works
adhere to this system, and this work is done by machinery driven by
either compressed air, hydraulic or electric power. In the first two
cases a scoop, filled with coal from an overhead hopper carried by the
travelling machine, is made to enter the retort and is turned over;
the operation is then repeated, but this time the scoop is turned over
in the opposite direction, the coal thus assuming such a position that
as much of its under surface as possible is exposed to the heated side
of the retort. With "through" retorts charging machines feed the
retorts at both ends, the scoop, which has a capacity of about 1-1/2
cwt., entering and discharging its contents twice at each end, so that
the total charge is about 6 cwt., which is allowed from four to six
hours to distil off according to the quality of the gas required. The
machines charge simultaneously at each end, so that the lids of the
retorts may be shut immediately the coal enters. The charging machines
travel on lines in front of the retort bench, and the power is
transmitted by connexions made with flexible hose. A device of more
recent introduction is an electrically-driven charging machine, in
which the centrifugal force created by a fly-wheel revolving at high
speed is applied to drive coal into the retort. If the velocity is
sufficiently high the coal may be carried the whole length of a 20-ft.
retort, the coal following banking up until an even layer is formed
throughout the length of the retort.
For the purpose of discharging the coke from the retort either
compressed air or hydraulic machinery is employed, a rake being made
to enter the retort and withdraw the coke on returning. With this
method it is necessary that the rake should enter and discharge
several times before the retort is clear, and thus the use of a
telescopic ram worked by hydraulic power, which pushes the coke before
it and discharges it at the other end, is an advantage. As much as
one-third on each ton of coal carbonized is saved by the use of
machinery in the retort-house. Taking into account the original cost
of such machines, and the unavoidable wear and tear upon the retorts
brought about by using labour-saving appliances, and the fact that the
coke-dust is very detrimental to the machinery, it is clear that the
suggestion of setting the retorts at an incline in order to facilitate
the work presented great inducements to the gas manager. The object
aimed at in thus setting retorts is to allow gravity to play the part
of charging and discharging the coal and coke, the retorts being
inclined at an angle to suit the slip of the class of coal used; this
angle is between 28 deg. and 34 deg. The coal, previously elevated to
hoppers, is dropped into the feeding chambers, which are so arranged
that they can travel from end to end of the retort-house and feed the
coal into the retorts. When the retort is to be charged, an iron stop
or barrier is placed in the lower mouthpiece, and the door closed. The
shoot is placed in the upper mouthpiece, and the stop or door, which
retains the coal in the chamber, is released; the coal is then
discharged into the retort, and rushing down the incline, is arrested
by the barrier, and banks up, forming a continuous backing to the coal
following. By experience with the class of coal used and the
adjustment of the stops in the shoot, the charge can be run into the
retort to form an even layer of any desired depth. For the withdrawal
of the residual coke at the end of the carbonization, the lower
mouthpiece door is opened, the barrier removed and the coke in the
lower part of the retort is "tickled" or gently stirred with an iron
rod to overcome a slight adhesion to the retort; the entire mass then
readily discharges itself. Guides are placed in front of the retort to
direct its course to the coke hoppers or conveyer below, and to
prevent scattering of the hot material. This system shows a greater
economy in the cost of carbonizing the coal, but the large outlay and
the wear and tear of the mechanical appliances involved have so far
prevented its very general adoption.
The vertical retort was one of the first forms experimented with by
Murdoch, but owing to the difficulty of withdrawing the coke, the low
illuminating power of the gas made in it, and the damage to the retort
itself, due to the swelling of the charge during distillation, it was
quickly abandoned. About the beginning of the 20th century, however,
the experiments of Messrs Settle and Padfield at Exeter, Messrs
Woodall and Duckham at Bournemouth, and Dr Bueb in Germany showed such
encouraging results that the idea of the vertical retort again came to
the front, and several systems were proposed and tried. The cause of
the failure of Murdoch's original vertical retort was undoubtedly that
it was completely filled with coal during charging, with the result
that the gas liberated from the lower portions of the retort had to
pass through a deep bed of red-hot coke, which, by over-baking the
gas, destroyed the illuminating hydrocarbons. There is no doubt that
the question of rapidly removing the gas, as soon as it is properly
formed, from the influence of the highly-heated walls of the retort
and residual coke, is one of the most important in gas manufacture.
In the case of horizontal retorts the space between the top of the
coal and the retort is of necessity considerable in order to permit
the introduction of the scoop and rake; the gas has therefore a free
channel to travel along, but has too much contact with the highly
heated surface of the retort before it leaves the mouthpiece. In the
case of inclined retorts this disadvantage is somewhat reduced, but
with vertical retorts the ideal conditions can be more nearly
approached. The heating as well as the illuminating value of the gas
per unit volume is lowered by over-baking, and Dr Bueb gives the
following figures as to the heating value of gas obtained from the
same coal but by different methods of carbonization:--
Vertical Retorts, 604 British thermal units per cub. ft.
Inclined " 584 " " "
Horizontal " 570 " " "
Of the existing forms of vertical retort it remains a matter to be
decided whether the coal should be charged in bulk to the retort or
whether it should be introduced in small quantities at regular and
short intervals; by this latter means (the characteristic feature of
the Settle-Padfield process) a continuous layer of coal is in process
of carbonization on the top, whilst the gas escapes without contact
with the mass of red-hot coke, a considerable increase in volume and
value in the gas and a much denser coke being the result.
Hydraulic main.
From the retort the gas passes by the ascension pipe to the hydraulic
main (fig. 7). This is a long reservoir placed in a horizontal
position and supported by columns upon the top of the retort stack,
and through it is maintained a slow but constant flow of water, the
level of which is kept uniform. The ascension pipe dips about 2 in.
into the liquid, and so makes a seal that allows of any retort being
charged singly without the risk of the gas produced from the other
retorts in the bench escaping through the open retort. Coal gas,
being a mixture of gases and vapours of liquids having very varying
boiling points, must necessarily undergo physical changes when the
temperature is lowered. Vapours of liquids of high boiling point will
be condensed more quickly than those having lower boiling points, but
condensation of each vapour will take place in a definite ratio with
the decrease of temperature, the rate being dependent upon the boiling
point of the liquid from which it is formed. The result is that from
the time the gaseous mixture leaves the retort it begins to deposit
condensation products owing to the decrease in temperature.
Condensation takes place in the ascension pipe, in the arch piece
leading to the hydraulic main, and to a still greater extent in the
hydraulic main itself where the gas has to pass through water.
[Illustration: FIG. 7.--Hydraulic Main.]
Ascension pipes give trouble unless they are frequently cleared by an
instrument called an "auger," whilst the arch pipe is fitted with hand
holes through which it may be easily cleared in case of stoppage. The
most soluble of the constituents of crude coal gas is ammonia, 780
volumes of which are soluble in one volume of water at normal
temperature and pressure, and the water in the hydraulic main absorbs
a considerable quantity of this compound from the gas and helps to
form the ammoniacal liquor, whilst, although the liquor is well
agitated by the gas bubbling through it, a partial separation of tar
from liquor is effected by gravitation. The liquor is run off at a
constant rate from the hydraulic main to the store tank, and the gas
passes from the top of the hydraulic main to the foul main.
Condensation.
The gas as it leaves the hydraulic main is still at a temperature of
from 130 deg. to 150 deg. F., and should now be reduced as nearly as
possible to the temperature of the surrounding atmosphere. The
operation of efficient condensing is not by any means as simple as
might be supposed. The tar and liquor when condensed have a dissolving
action on various valuable light-giving constituents of the gas, which
in the ordinary way would not be deposited by the lowering of
temperature, and for this reason the heavy tar, and especially that
produced in the hydraulic main, should come in contact with the gas as
little as possible, and condensation should take place slowly.
The main difficulty which the condenser ought to overcome and upon
which its efficiency should depend is the removal of naphthalene: this
compound, which is present in the gas, condenses on cooling to a solid
which crystallizes out in the form of white flakes, and the trouble
caused by pipe stoppages in the works as well as in the district
supplied is very considerable. The higher the heat of carbonization
the more naphthalene appears to be produced, and gas managers of
to-day find the removal of naphthalene from the gas a difficult
problem to solve. It was for some time debated as to whether
naphthalene added materially to the illuminating value of the gas, and
whether an endeavour should be made to carry it to the point of
combustion; but it is now acknowledged that it is a troublesome
impurity, and that the sooner it is extracted the better. Gas leaves
the retorts saturated with naphthalene, and its capacity for holding
that impurity seems to be augmented by the presence of water vapour.
The condenser, by effecting the condensation of water vapour, also
brings about the deposition of solid naphthalene, apart from that
which naturally condenses owing to reduction of temperature.
Condensers are either air-cooled or water-cooled, or both. In the
former case the gas traverses pipes exposed to the atmosphere and so
placed that the resulting products of condensation may be collected at
the lowest point. Water is a more efficient cooling medium than air,
owing to its high specific heat, and the degree of cooling may be more
easily regulated by its use. In water-cooled condensers it is usual to
arrange that the water passes through a large number of small pipes
contained in a larger one through which the gas flows, and as it
constantly happened that condenser pipes became choked by naphthalene,
the so-called reversible condenser, in which the stream of gas may be
altered from time to time and the walls of the pipes cleaned by
pumping tar over them, is a decided advance.
The solubility of naphthalene by various oils has led some engineers
to put in naphthalene washers, in which gas is brought into contact
with a heavy tar oil or certain fractions distilled from it, the
latter being previously mixed with some volatile hydrocarbon to
replace in the gas those illuminating vapours which the oil dissolves
out; and by fractional distillation of the washing oil the naphthalene
and volatile hydrocarbons are afterwards recovered.
Exhauster.
The exhauster is practically a rotary gas pump which serves the
purpose of drawing the gas from the hydraulic main through the
condensers, and then forcing it through the purifying vessels to the
holder. Moreover, by putting the retorts under a slight vacuum, the
amount of gas produced is increased by about 12%, and is of better
quality, owing to its leaving the heated retort more quickly. A
horizontal compound steam-engine is usually employed to drive the
exhauster.
At this point in the manufacturing process the gas has already
undergone some important changes in its composition, but there yet
remain impurities which must be removed, these being ammonia,
sulphuretted hydrogen, carbon disulphide and carbon dioxide. Ammonia
is of considerable marketable value, and even in places where the
local Gas Act does not prescribe that it shall be removed, it is
extracted. Sulphuretted hydrogen is a noxious impurity, and its
complete removal from the gas is usually imposed by parliament. As
nearly as possible all the carbon dioxide is extracted, but most gas
companies are now exempt from having to purify the gas from sulphur
compounds other than sulphuretted hydrogen. Cyanogen compounds also
are present in the gas, and in large works, where the total quantity
is sufficient, their extraction is effected for the production of
either prussiate or cyanide of soda.
Atkinson Butterfield gives the composition of the gas at this point to
be about
per cent. by vol.
Hydrogen from 42 to 53
Methane " 32 " 39
Carbon monoxide " 3 " 10
Hydrocarbons--
Gases " 2.5 " 4.5
Light condensable
vapours " 0.5 " 1.2
Carbon dioxide " 1.1 " 1.8
Nitrogen " 1.0 " 5.0
Sulphuretted hydrogen " 1.0 " 2.0
Ammonia " 0.5 " 0.95
Cyanogen " 0.05 " 0.12
Carbon disulphide " 0.02 " 0.035
Naphthalene " 0.005 " 0.015
Washers.
It happens that ammonia, being a strong base, will effect the
extraction of a certain proportion of such compounds as sulphuretted
hydrogen, carbon dioxide and hydrocyanic acid, and the gas is now
washed with water and ammoniacal liquor. The process is termed washing
or scrubbing, and is carried out in various forms of apparatus, the
efficiency of which is dependent upon the amount of contact the
apparatus allows between the finely divided gas and water in a unit
area and the facility with which it may be cleared out. The "Livesey"
washer, a well-known type, is a rectangular cast iron vessel. The gas
enters in the centre, and to make its escape again it has to pass into
long wrought iron inverted troughs through perforations one-twentieth
of an inch in diameter. A constant flow of liquor is regulated through
the washer, and the gas, in order to pass through the perforations,
drives the liquor up into the troughs. The liquor foams up owing to
agitation by the finely divided streams of gas, and is brought into
close contact with it. Two or three of these washers are connected in
series according to the quantity of gas to be dealt with.
Scrubbers.
The final washing for ammonia is effected in an apparatus termed a
"scrubber," which is a cylindrical tower packed with boards 1/4 in.
thick by 11 in. broad, placed on end and close together; water is
caused to flow down over the surface of these boards, the object being
to break up the gas as much as possible and bring it into close
contact with the water. In this wet purifying apparatus the gas is
almost wholly freed from ammonia and from part of the sulphuretted
hydrogen, whilst carbon dioxide and carbon disulphide are also
partially extracted.
[Illustration: FIG. 8.--Purifier.]
Purifiers.
The final purification is carried out in rectangular vessels, known as
"dry purifiers" (fig. 8). Internally, each purifier is filled with
ranges of wooden trays or sieves A, made in the form of grids (fig.
9), and covered with the purifying material B to a depth of about 6
in., the number of tiers and size of purifier boxes being proportional
to the quantity of gas to be purified. The gas enters at the bottom by
the pipe C, the inlet being protected from any falling material by the
cover D; it forces its way upwards through all the trays until,
reaching the lid or cover E, it descends by the exit tube F, which
leads to the next purifier. The edges of the lid dip into an external
water seal or lute G, whereby the gas is prevented from escaping.
[Illustration: FIG. 9.--Purifier Grid.]
When the gas had to be purified from carbon disulphide as well as from
sulphuretted hydrogen, slaked lime was employed for the removal of
carbon dioxide and the greater quantity of the sulphur compounds,
whilst a catch box or purifier of oxide of iron served to remove the
last traces of sulphuretted hydrogen. Not fewer than four lime
purifiers were employed, and as the one which was first in the series
became exhausted, i.e. began to show signs of allowing carbon dioxide
to pass through it unabsorbed, it was filled with fresh slaked lime
and made the last of the series, the one which was second becoming
first, and this procedure went on continuously. This operation was
necessitated by the fact that carbon dioxide has the power of breaking
up the sulphur compounds formed by the lime, so that until all carbon
dioxide is absorbed with the formation of calcium carbonate, the
withdrawal of sulphuretted hydrogen cannot proceed, whilst since it is
calcium sulphide formed by the absorption of sulphuretted hydrogen by
the slaked lime that absorbs the vapour of carbon disulphide,
purification from the latter can only be accomplished after the
necessary calcium sulphide has been formed. The foul gas leaving the
scrubbers contains, as a general average, 30 grains of sulphuretted
hydrogen, 40 grains of carbon disulphide and 200 grains of carbon
dioxide per 100 cub. ft. On entering the first purifier, which
contains calcium thiocarbonate and other combinations of calcium and
sulphur in small quantity, the sulphuretted hydrogen and disulphide
vapour have practically no action upon the material, but the carbon
dioxide immediately attacks the calcium thiocarbonate, forming calcium
carbonate with the production of carbon disulphide vapour, which is
carried over with the gas into the second box. In the connexion
between the first and the second box the gas is found to contain 500
grains of sulphuretted hydrogen and 80 grains of carbon disulphide per
100 cub. ft., but no trace of carbon dioxide. In the second box the
formation of calcium thiocarbonate takes place by the action of carbon
disulphide upon the calcium sulphide with the liberation of
sulphuretted hydrogen, which is carried over to the third purifier.
The gas in the connecting pipe between the second and third purifier
will be found to contain 400 grains of sulphuretted hydrogen and 20
grains of carbon disulphide. The contents of the third box, being
mostly composed of slaked lime, take up sulphuretted hydrogen forming
calcium sulphide, and practically remove the remaining impurities, the
outlet gas showing 20 grains of sulphuretted hydrogen and 8 grains of
carbon disulphide per 100 cub. ft., whilst the catch box of oxide of
iron then removes all traces of sulphuretted hydrogen. It will be
noticed that in the earlier stages the quantity of sulphur impurities
is actually increased between the purifiers--in fact, the greater
amount of sulphiding procures the ready removal of the carbon
disulphide,--but it is the carbon dioxide in the gas that is the
disturbing element, inasmuch as it decomposes the combinations of
sulphur and calcium; consequently it is a paramount object in this
system to prevent this latter impurity finding its way through the
first box of the series. The finding of any traces of carbon dioxide
in the gas between the first two boxes is generally the signal for a
new clean purifier being put into action, and the first one shut off,
emptied and recharged with fresh lime, the impregnated material being
sometimes sold for dressing certain soils.
The action of oxide of iron, which has now partly replaced the lime
purification, depends on its power of combining with sulphuretted
hydrogen to form sulphide of iron. Such is the affinity of the oxide
for this impurity that it may contain from 50 to 60% by weight of free
sulphur after revivification and still remain active. Upon removing
the material from the vessel and exposing it to the atmosphere the
sulphide of iron undergoes a revivifying process, the oxygen of the
air displacing the sulphur from the sulphide as free sulphur, and with
moisture converting the iron into hydrated oxide of iron. This
revivification can be carried on a number of times until the material
when dry contains about 50% of free sulphur and even occasionally 60%
and over; it is then sold to manufacturers of sulphuric acid to be
used in the sulphur kilns instead of pyrites (see SULPHURIC ACID).
Apart from the by-products coke, coke-breeze, tar and retort carbon,
which are sold direct, gas companies are now in many cases preparing
from their spent purifying material pure chemical products which are
in great demand. The most important of these is sulphate of ammonia,
which is used for agricultural purposes as a manure, and is obtained
by passing ammonia into sulphuric acid and crystallizing out the
ammonium sulphate produced. To do this, saturated ammoniacal liquor is
decomposed by lime in the presence of steam, and the freed ammonia is
passed into strong sulphuric acid, the saturated solution of ammonium
sulphate being carefully crystallized. The market value of the salt
varies, but an average figure is L12 per ton, whilst the average yield
is about 24 lb. of salt per ton of coal carbonized. In large works the
sulphuric acid is usually manufactured on the spot from the spent
oxide, so that the sulphuretted hydrogen, which in the gas is
considered an undesirable impurity, plays a valuable part in the
manufacture of an important by-product.
Cyanogen compounds are extracted either direct from the gas, from the
spent oxide or from ammoniacal liquor, and some large gas works now
produce sodium cyanide, this being one of the latest developments in
the gas chemical industry.
[Illustration: FIG. 10.--Gasholder.]
[Illustration: FIG. 11.--Cup and Grip.]
Gasholder.
The purified gas now passes to a gasholder (sometimes known as a
gasometer), which may be either single lift, i.e. a simple bell
inverted in a tank of water, or may be constructed on the telescopic
principle, in which case much ground space is saved, as a holder of
much greater capacity can be contained in the same-sized tank. The
tank for the gasholder is usually made by excavating a circular
reservoir somewhat larger in diameter than the proposed holder. A
banking is allowed to remain in the centre, as shown in fig. 10, which
is known as the "dumpling," this arrangement not only saving work and
water, but acting as a support for the king post of a trussed holder
when the holder is empty. The tank must be water-tight, and the
precaution necessary to be taken in order to ensure this is dependent
upon the nature of the soil; it is usual, however, for the tanks to be
lined with concrete. Where the conditions of soil are very bad, steel
tanks are built above ground, but the cost of these is much greater.
The holder is made of sheet iron riveted together, the thickness
depending upon the size of the holder. The telescopic form consists of
two or more lifts which slide in one another, and may be described as
a single lift holder encircled by other cylinders of slightly larger
diameter, but of about the same length. Fig. 10 shows the general
construction. Gas on entering at A causes the top lift to rise; the
bottom of this lift being turned up all round to form a cup, whilst
the top of the next lift is turned down to form a so-called grip, the
two interlock (see fig. 11), forming what is known as the hydraulic
cup. Under these conditions the cup will necessarily be filled with
water, and a seal will be formed, preventing the escape of gas. A
guide framing is built round the holder, and guide rollers are fixed
at various intervals round the grips of each lift, whilst at the
bottom of the cup guide rollers are also fixed (fig. 11). In the year
1892 the largest existing gasholder was built at the East Greenwich
works of the South Metropolitan Gas Company; it has six lifts, its
diameter is 293 ft., and when filled with gas stands 180 ft. high. The
capacity for gas is 12 million cub. ft.
Governor.
The governor consists usually of a bell floating in a cast iron tank
partially filled with water, and is in fact a small gasholder, from
the centre of which is suspended a conical valve controlling the gas
inlet and closing it as the bell fills. Any deviation in pressure will
cause the floating bell to be lifted or lowered, and the size of the
inlet will be decreased or increased, thus regulating the flow.
Enrichment.
The fact that coal gas of an illuminating power of from 14 to 16
candles can be made from the ordinary gas coal at a fairly low rate,
while every candle power added to the gas increases the cost in an
enormous and rapidly growing ratio, has, from the earliest days of
the gas industry, caused the attention of inventors to be turned to
the enrichment of coal gas. Formerly cannel coal was used for
producing a very rich gas which could be mixed with the ordinary gas,
thereby enriching it, but as the supply became limited and the price
prohibitive, other methods were from time to time advocated to replace
its use in the enrichment of illuminating gas. These may be classified
as follows:--
1. Enriching the gas by vapours and permanent gases obtained by
decomposing the tar formed at the same time as the gas.
2. Mixing with the coal gas oil gas, obtained by decomposing crude
oils by heat.
3. The carburetting of low-power gas by impregnating it with the
vapours of volatile hydrocarbons.
4. Mixing the coal gas with water gas, which has been highly
carburetted by passing it with the vapours of various hydrocarbons
through superheaters in order to give permanency to the hydrocarbon
gases.
Enrichment by tar.
Very many attempts have been made to utilize tar for the production
and enrichment of gas, and to do this two methods may be adopted:--
(a) Condensing the tar in the ordinary way, and afterwards using the
whole or portions of it for cracking into a permanent gas.
(b) Cracking the tar vapours before condensation by passing the gas
and vapours through superheaters.
If the first method be adopted, the trouble which presents itself is
that the tar contains a high percentage of pitch, which tends rapidly
to choke and clog up all the pipes. A partly successful attempt to
make use of certain portions of the liquid products of distillation of
coal before condensation by the second method was the Dinsmore
process, in which the coal gas and vapours which, if allowed to cool,
would form tar, were made to pass through a heated chamber, and a
certain proportion of otherwise condensible hydrocarbons was thus
converted into permanent gases. Even with a poor class of coal it was
claimed that 9800 cub. ft. of 20- to 21-candle gas could be made by
this process, whereas by the ordinary process 9000 cub. ft. of
15-candle gas would have been produced. This process, although
strongly advocated by the gas engineer who experimented with it, was
never a commercial success. The final solution of the question of
enrichment of gas by hydrocarbons derived from tar may be arrived at
by a process which prevents the formation of part of the tar during
the carbonization of the coal, or by the process devised by C.B. Tully
and now in use at Truro, in which tar is injected into the
incandescent fuel in a water-gas generator and enriches the water gas
with methane and other hydrocarbons, the resulting pitch and carbon
being filtered off by the column of coke through which the gas passes.
Enrichment by oil gas.
The earliest attempts at enrichment by oil gas consisted in spraying
oil upon the red hot mass in the retort during carbonization; but
experience soon showed that this was not an economical method of
working, and that it was far better to decompose the liquid
hydrocarbon in the presence of the diluents which are to mingle with
it and act as its carrier, since, if this were done, a higher
temperature could be employed and more of the heavier portions of the
oil converted into gas, without at the same time breaking down the
gaseous hydrocarbons too much. In carburetting poor coal gas with
hydrocarbons from mineral oil it must be borne in mind that, as coal
is undergoing distillation, a rich gas is given off in the earlier
stages, but towards the end of the operation the gas is very poor in
illuminants, the methane disappearing with the other hydrocarbons, and
the increase in hydrogen being very marked. Lewis T. Wright employed a
coal requiring six hours for its distillation, and took samples of the
gas at different periods of the time. On analysis these yielded the
following results:--
_Time after beginning Distillation._
+------------------------+----------+------------+------------+------------+
| | 10 | 1 hour | 3 hours | 5 hours |
| | minutes. | 30 minutes.| 25 minutes.| 35 minutes.|
+------------------------+----------+------------+------------+------------+
| Sulphuretted hydrogen | 1.30 | 1.42 | 0.49 | 0.11 |
| Carbon dioxide | 2.21 | 2.09 | 1.49 | 1.50 |
| Hydrogen | 20.10 | 38.33 | 52.68 | 67.12 |
| Carbon monoxide | 6.19 | 5.66 | 6.21 | 6.12 |
| Saturated hydrocarbons | 57.38 | 44.03 | 33.54 | 22.58 |
| Unsaturated " | 10.62 | 5.98 | 3.04 | 1.79 |
| Nitrogen | 2.20 | 2.47 | 2.55 | 0.78 |
+------------------------+----------+------------+------------+------------+