SECTION II.--RAW MATERIALS AND PRELIMINARY TREATMENT

The raw materials for the manufacture of gelatine and glue may be

classified according to their origin. The preliminary treatment, which

comprises chiefly purifying and cleansing operations, is varied

according to type of manufacturing process for which it is a

preparation.

In the case of hide or =skin gelatine=, the raw material is a

bye-product of the leather industry. After the hides or skins have

passed through the preparatory processes which convert them into "pelt"

(see Part I., Section II.), they are so trimmed that all that is left

will make a useful leather. These "trimmings" or "roundings" include

ears and noses, the udders of cows and heifers, and also include parts

from the butt, belly and shanks which are collectively termed "pieces."

The operation of fleshing (Part I., Section II.), in which fat and flesh

are cut from that side of the hides and skins which was next the flesh,

also involves cutting into the collagen to some extent, and these

"fleshings" comprise another very large class of raw material. The

fleshings obtained by hand labour contain distinctly more hide

substances than those obtained by machine work, and their commercial

value to the gelatine manufacturer is of course proportionate to the

collagen content. Some hides and skins are split in the pelt (Part I.,

Section IX.; Part II., Sections II., III. and IV.), and the "flesh

split," though sometimes made into leather, is also used in making

gelatine, a high quality being obtained from such material. Minor

sources of material are tendons and cartilages, and also hides and skins

which have been too much damaged by partial putrefaction or by accidents

to make sound leather. Of course the material from the hides for heavy

leathers form the greater bulk of raw material for skin gelatine which

is thus derived principally from ox hides but sheep and goat skin pieces

have also an important place. The skins of other animals, such as dogs,

cats, hares and rabbits not usually made into leather can also be

depilated and used for making skin gelatine and glue. Horse hide

fleshings and pieces are sometimes used, but are notorious for the poor

quality of their product. They seem to contain less [alpha] gelatin. All

these materials are of course readily putrescible and must be put "into

work" without much loss of time. When it is impossible to convey them

from the tannery to the gelatine factory quickly enough, _e.g._ foreign

material, the "glue stock" is dried out completely and sold in that

condition. In the manufacture of pickers from limed pelt there is some

superfluous material, and this is cut into shavings and dried. This

"picker waste" also forms a useful source of raw material. Skin gelatine

material is not very strong in gelatine-substance. The fleshings,

pieces, etc., contain much water, even up to 80 per cent. This, however,

is very variable, and only a practical test or a hide substance

determination can indicate the commercial value of any particular

material. This value, moreover, is determined not only by the yield and

quality of the gelatine which can be obtained, but also by the yield of

grease, the valuable bye-product.

The preliminary treatment of material for skin gelatine consists

essentially of liming and of washing. The object of each process is to

purify. Liming has much the same action on hide pieces, etc., as on

hides, and indeed the liming treatment is somewhat superfluous on

cuttings from well-limed hides. The material is plumped up and the

partially hydrolyzed products are taken into solution. Lime also acts as

mild antiseptic, stops any putrefaction and liberates ammonia formed by

fermentation in transit to the factory. When plumping is particularly

wanted (as in wetting in dry stock) caustic soda is sometimes used as an

assistant (_cf._ dried hides). Sodium sulphide has also been used

for this purpose. The liming is in brick pits, an excess of undissolved

lime being always used. It is advantageous frequently to disturb or

agitate the goods in the lime pits. Up to ten weeks liming has sometimes

been given, but about three weeks is now generally considered

sufficient, and the tendency is to shorten the time. The lime and soda

have also a detergent action on soiled stock, and they probably assist

in hydrolyzing the pigments of the hair roots and sheaths. They also

saponify and emulsify the grease, and it is obvious, therefore, that

liming can be carried too far. Slaked lime, of course, must always be

used.

After liming the soaked, softened and plumped stock is washed as

thoroughly as possible. To do this it is necessary to supply repeated

batches of clean cold water. Some manufacturers, however, use the warm

water from the evaporators. Wooden vats or brick pits with arrangements

for agitation, for draining off and for inspection, are used for this

purpose. The agitation may be carried out by means of revolving shafts

or drums with projecting curved spokes or vanes. An American patent

(Hoeveler's glue stock washer) involves the use of a paddle wheel. It is

combined with a settling tank to gather particles of stock. In the

washing the chalk, excess lime, dirt, etc., are quickly removed and a

slow deliming process is commenced. The sediment from the washers and

wash waters has some value in making fertilizers. Deliming cannot be

carried on further than certain limits by water alone. Hence acid is

often added to finish off the process. Hydrochloric acid has the

advantage of forming soluble salts, but if they are not removed

completely their lyotrope influence is to weaken the gelatine. Sulphuric

and sulphurous acids are even cheaper, and the lyotrope influence of

their salts is in the opposite sense. The latter also has the advantage

of destroying sulphides, an important advantage for food gelatines.

Whatever acid is used, however, it is evident that an abundance of pure

cold water is the fundamental requirement of a pure product. It is a

sound maxim in gelatine manufacture to avoid, if at all possible, the

addition of any soluble substance, for it is always present in a more

concentrated state in the finished article. Thus if its solubility be

even moderate, one is likely to attain supersaturation in the "cake"

and consequently a dull product. Further, lyotrope influences can never

strengthen a gel very much, but may and often do weaken it very

considerably. Hence the aim of most manufacturers in the preliminary

treatment is so to delime that a nearly neutral and salt-free product is

obtained. An exception is the case of skin gelatine in which excess of

sulphurous acid is used. This process has for its object not only

deliming and purifying, but also a bleaching action.

In the case of =bone gelatine=, the raw material is such that there are

much longer and more elaborate preparatory processes. This arises from

the fact that about half the bones of animals consists of mineral

matter, chiefly calcium phosphate. Bones, of course, vary in composition

to some extent, and those from younger animals contain distinctly less

of the mineral constituents. Approximately speaking, bones have the

following average composition:--

Gelatinous matter 21-1/2 per cent.

Fat 12-1/2 " "

Calcium phosphate 48 " "

Calcium carbonate 3 " "

Alkali salts, silica, etc. 2-1/2 " "

Water 12-1/2 " "

--------

100 " "

It will be seen, therefore, that the manufacture of bone gelatine and of

a comparatively large proportion of phosphate involves the recovery and

purification of much fatty matter. The manufacturing processes are

naturally subject to considerable variation. One respect in which they

differ is the stage in which grease is removed. Sometimes this is simply

done as the need and occasion arise, and it is skimmed out in the acid

or water extractions, but it is now more usual to have a special

"degreasing" process. There are, moreover, two quite distinct types of

manufacture. In one of these (the boiling process) the routine bears

some resemblance to that for skin gelatine. In this process the bones

are washed and cleansed and then immediately subjected to extraction

with water. This removes the gelatinous matter and leaves the phosphate

and earthy matters behind. Grease may be removed before the water

extraction, but is also sometimes removed by skimming off during the

extraction, as is usual in the case of skin gelatine. This procedure is

now not much favoured unless only a low-grade glue is required. In the

other type of manufacture (the acid process) the material is first

degreased, and then the mineral matter is extracted or dissolved by

acids, leaving the gelatinous matter behind for subsequent refinement

and solution. The acid process has long been preferred for high-class

bone gelatine, and hence needs further discussion.

The degreasing operation was once brought about by steaming only, but is

now accomplished with the assistance of fat solvents.

The object of cleansing is not only to remove dirt, but also fleshy

matter which often adheres to the bones. This may contain a little

gelatine, but consists mainly of other proteins and insoluble fibre,

neither of which are wanted in the water extraction. The mill consists

of a large cylinder of stout wire gauze. This revolves round the axis of

the cylinder, and the bones are fed in at one end by a hopper and are

discharged at the other. The revolution of the mill causes the friction

which polishes off the fleshy matter. The dirt and flesh fall through

the gauze and are sent to the fertilizer factory. The polishings are

sometimes further separated by a similar machine. Raw bones may thus

yield nearly 60 per cent. of degreased bones, and about 56 per cent.

cleansed bones ready for extraction, and 3 or 4 per cent. "bone meal."

The next stage is the extraction of the mineral matters by acid, for

which purpose hydrochloric acid has proved very suitable, as both

phosphate and carbonate of lime are dissolved by it. The usual

counter-current system of extraction is used [_cp._ Leaching and extract

manufacture, Part I., Section III., p. 35]. The process is methodical

and regular, the acid liquor passing successively through a battery

of six vats in such a manner that the liquor richest in lime salts comes

into contact with the bones most recently charged; the fresh acid thus

acts upon the nearly extracted bones. The hydrochloric acid used is of 8

to 10 per cent. strength (5° to 7° Bé.). Stronger acid is apt to

hydrolyze ("rot") the gelatine, whilst weaker acid takes longer time.

The process takes 8 to 10 days, though up to 14 days is sometimes given,

and, on the other hand, the process has been occasionally reduced to 4

days. The gelatinous matter undissolved has the shape of the original

bone, but is much swollen. When the acid liquor is saturated with lime

salt, the liquor is drawn off from below the vats and sent to the

phosphate precipitation tanks. The phosphate is usually precipitated by

adding just sufficient milk of lime to neutralize the hydrochloric acid.

The precipitated phosphate is then well washed by decantation to remove

calcium chloride. It is then drained, and dried at a low temperature. As

a large bulk of phosphate is obtained it is often filter-pressed and

dried quickly in long revolving chambers through which a current of air

is passed. The phosphate is sometimes also precipitated by ammonia. It

is then more easily washed and dried, and the ammonium chloride is

recovered and may be used to regenerate ammonia, or be sold as a

valuable bye-product. Sometimes the acid liquor is not used for making

precipitated phosphate, but is evaporated with animal charcoal and

silica and then distilled to make phosphorus.

The next stage is the purification by washing of the gelatinous matter

which remains. The vat is filled up with pure cold water and the

material allowed to steep for six or seven hours. The acid and salts

remaining diffuse outwards into the water. This is drained off and

replaced by fresh water, and the procedure repeated half a dozen times

or as often as necessary. The end is said to be determined by the

absence of a precipitate on adding silver nitrate to the wash water, or

by the absence of any action on blue litmus paper. It will be seen,

however, that there are two actions involved, one being the removal of

calcium chloride and the other the removal of excess acid. The former

is the easier, and is almost necessarily brought about by the latter.

Hence in some factories the neutralization is brought about, therefore,

by the addition of a certain quantity of soda, or more usually by lime,

and the material is sometimes submitted to a veritable liming by which

it remains in milk of lime for about three weeks, the lime liquor being

renewed several times. The product is finally washed again to remove

excess lime. This is carried out in a rotating vessel through which

passes a continuous stream of water. If a slightly acid gelatine is

required, however, the lime and liming are both superfluous, and the

procedure is simply to wash as thoroughly as possible and then to

immerse the material in a 1 per cent. sulphurous acid solution for 3

hours to bleach, and then to proceed with the water extraction or

solution of the gelatine. The hydrochloric acid used for these processes

should be as pure as possible, and the degreasing as thorough as

possible, for, if not, a gelatine with a bad odour is liable to be

obtained.

Instead of using hydrochloric acid for the solution of mineral matter,

sulphurous acid is sometimes employed, and has the advantages that its

bleaching effect is thereby obtained throughout the process, and that it

is recoverable for subsequent use. The Bergmann process, most generally

favoured, is described very concisely by Rideal thus: "A sulphurous acid

solution is made to circulate over the bones in a series of closed

tanks, the solution being continually enriched with sulphurous acid from

a cylinder of the liquefied gas. The resulting liquor, containing an

acid calcium phosphate and calcium bisulphite, is heated by steam in a

leaden digestor, when the excess of sulphurous acid is liberated and

passes back to the tanks, while neutral calcium phosphate and sulphite

are precipitated. The latter is decomposed by an equivalent of

hydrochloric acid, setting free the remaining sulphurous acid, which is

returned to the tanks, leaving calcium chloride in solution, and neutral

calcium phosphate in suspension." Not more than 5 per cent. of

sulphurous acid is said to be lost in this process, and the gelatine is

more thoroughly bleached. It is subsequently well washed before

extraction.

=Recovery and Purification of Grease.=--The degreasing operation, which

is applied usually to bones and to skin glue scutch, was once brought

about by steaming only, but is now accomplished with the assistance of

fat solvents, though in the latter case steaming together with

mechanical centrifugal force has proved sufficiently successful. On the

Continent carbon disulphide was once largely used as solvent, and in

this country benzene has been employed, but their low volatility and

high inflammability, as well as their expense, make both these

substances somewhat unsuitable, and it is now usual to make use of

petroleum oils, whether Scotch, American or Russian. A fraction which

boils about the same temperature as water is usually employed, and all

of it must be volatile under 280° F. Before the actual grease extraction

the bones should be sorted over and unsuitable substances (horns,

gravel, iron, etc.) removed. They are also usually put through a mill

and roughly crushed or broken. The actual grease extraction plant

consists of large copper vessels which will each take 5 tons of bones.

These extractors are arranged in sets so that the degreasing is

proceeding in some whilst the others are being emptied and recharged.

The doors for charging and emptying must be securely fastened. When the

extractor is charged the solvent is run in and heated by a steam coil

which eventually causes it to distil. After some hours the remainder,

which has dissolved much grease, is run off, and a fresh lot of solvent

is added and heated up. After four such extractions only about 1/4 per

cent. of grease remains in the bones. To remove the remainder of the

solvent high-pressure steam (80 lbs.) is blown through the bones. The

extractor is then opened and the degreased and somewhat dried bones are

mechanically conveyed to the cleansing mill. The grease solutions

obtained are subjected again to steam with a view to removing the

solvent and obtaining it for repeated use in this sense. The efficient

distillation and recovery of the solvent is indeed an essential element

in the success of the process.

The greases obtained, whether by the use of fat solvents or by skimming

off during extraction, or in any other way, are mixed together as is

appropriate to their origin and purity, and subjected to further

purification, the object of which is to remove gelatinous and albuminous

matters, and to decompose lime or soda soaps. The precise methods of

purification are, of course, dependent mainly upon the impurities known

to be present, but the readiest method is to give the grease further

steaming or boiling with water, and so effect by washing and by solvent

action the elimination of non-fatty matters. In many cases it is found

advantageous to employ mineral acids or oxidizing agents to assist the

process. The process may be repeated as often as is desired.

The recovered and purified greases are often of a high standard of

purity, and the best are quite fit for edible purposes. The large

extension of the margarine industry in this country has indeed caused a

larger proportion than ever of this bye-product to be so used. In some

cases it is found commercially advantageous to submit the grease to

action of the filter press, and so to separate it into solid and liquid

portions, the former containing a much larger proportion of stearin, and

the latter of olein. Much of the grease from the gelatine trade is also

found suitable for soap manufacture, and is therefore a valuable source

of glycerine.

=Other Raw Materials.=--Whilst hide pieces and fleshings, and animal

bones, comprise the principal raw material for the manufacture of

gelatine and glue, there are also minor sources of raw material which,

though often not suitable for gelatine manufacture, will yield a

satisfactory glue. Thus the skins, bladders and bones of fish form the

source of "fish glue." Sole skins, indeed, when deodorized by chlorine

and decolorized by animal charcoal, are made into gelatine. The bladders

of some fish (_e.g._ the sturgeon) are washed, purified and dried with

rolling to make "isinglass," a form of natural gelatine in which the

original fibrous structure is retained. There is a limited demand for

this material for clarifying purposes by brewers, wine merchants and

cooks.

Leather waste may sometimes be used to make a low-grade glue.

Vegetable-tanned leather offers much difficulty unless very lightly and

recently tanned. The tannage must be stripped by drumming with weak

alkalies, _e.g._ borax, sodium sulphite, or weak soda. Chrome leather

may be stripped easily and completely by Rochelle salt and other salts

of hydroxy acids (Procter and Wilson), and also by ammonia acetate,

oxalate and similar salts (Bennett), also by certain organic acids

(Lamb). Processes are patented by which chrome leather is digested with

lime to make glue, the chromium hydrate being insolubilized. Viscous and

tenacious substances are also obtained from some vegetable matters and

are called "glue."

REFERENCES.

"Glue and Glue Testing," S. Rideal, D.Sc., 2nd ed.; Skin Gelatine

and Glue, pp. 25-48; Bone Gelatine and Glue, pp. 59-66.

"Gelatine, Glue and their Allied Products," T. Lambert, pp. 11-52.

"Encyclopedie chimique," Fremy, tome x.

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