US1845487A

US1845487A - Method for the production of pulp

Info

Publication number: US1845487A
Application number: US287651A
Authority: US
Inventors: Elton R Darling
Original assignee: CORNSTALK PRODUCTS Co Inc
Current assignee: CORNSTALK PRODUCTS Co Inc; CORNSTALK PRODUCTS COMPANY Inc
Priority date: 1928-06-22
Filing date: 1928-06-22
Publication date: 1932-02-16
Anticipated expiration: 1949-02-16
Also published as: GB314061A

Description

Patented Feb. 16, 1932 UNITED STATES PATENT; OFFICE ELTON R. DARLING, OF DECATUR, ILLINOIS, ASSIGNOB, IBY MESNE ASSIGNMENTS, TO

COR-NSTALK PRODUCTS COMPANY, INC.,

DELAWARE OF NEW YORK, N. Y., A CORPORATION 01'! METHOD FOR THE PRODUCTION OF PULP No Drawing.

This invention relates to the production of pulp suitable for any of the many uses for which pulp of the usual type is adapted, and has especial reference to the production of pulp from many of what have been considered the wastes of agriculture containin a low lignin content and relatively high amounts of pentosans.

Among the vegetable growths in this class may be included cornstalks, bagasse, rice, and

wheat straw, together with corn cobs, oathulls, rice hulls, cottonseed hulls, etc., etc.

There have been many methods devised for the pulping of these low lignin content and high pentosan content materials; but as will be seen in the disclosure hereinafter, the meth- 0d of this application is new, and involves great economy and features which permit of the production of s ecialty ulps and paper at a, great saving 0 time, la or and expense.

As is well known, the basic structure of the materials referred to hereinbefore is cellulose associated with other materials which can be separated from the cellulose in various ways, some of which involve deterioration of the cellulose, and others of which involve drastic treatment. The latter treatment frequently deteriorates the cellulose as well as the structure thereof from a physical standpoint.

lin the process of this application the treatment accorded the materlal is not drastic, the final product is obtained in a very satisfactory condition for many uses, and the cost of production is low, thereby permittingvcompet1tion with other pulps produced at a low cost, but lacking many of the desirable properties possessed by the cellulose obtained by this process. r

In workin some of the materials referred to above, suc as cornstalks, bagasse, etc., it is necessary to shred them to make them workable, and it has been found practical and desirable to co-ordinate a washing process with the said shredding process, so that dirt and foreign matter collected in the field may be removed at the same time.

The shredded and washed material is then fed into 'a digester, ten times its weight in water is added, the digester is closed and heat and pressure of approximately ten pounds is Application filed June 22,

that the water therein may be drawn out at the lower portion thereof, passed through a heater, and then sprayed into the top of the digester where it is sucked through the mass and again passed out of the digester at the bottom thereof.

This process is followed for a period of approximately thirty minutes, in which time any water soluble materials present are extracted and the fibre is opened and made more susceptible to the subsequent treatments.

As is well known the plant growths referred to herein as used in this process contain two types of pentosans, one of which types acts as reserve food material for the plant, the other type going to make up the structure of the plant, one of its functions being the binding together of .the fibres.

When these binding pentosans are "treated in a manner to convert them into soluble chemical products, their removal is not only easy, but frees the fibres, which may then be readily acted upon by certain chemicals to make the pulping operation easy of accomplishment.

This process of treating the pentosans may be termed hydrolysis and it has been found eflicient and economical in the use of same in connection with this process to employ a weak solution of sulphuric acid, for instance, one percent.

When the aforesaid hydrolysis operation is completed and pressure has been used, the pressure is released, the acid solution is drained oil", and the residual mass is washed to remove the acid.

Neither do I desire to be limited strictly to the use of sulphuric acid in the step of rendering soluble and removing the binding pentosans without damage to the fibre.

5 Other chemicals of a more costly nature could be used to equal advantage, but at greater expense, and, therefore, the sulphuric acid is preferable.

Having thus described my invention, what I claim and desire to secure by Letters Patent, is

1. The method of producin cellulosic pulp from vegetable rowths of ow lignin content and relative y higher pentosan content comprising the following steps; shredding and cleansing the material; digesting same in approximately ten times its weight of water and under heat and pressure; drawing off the water, heating same and passing it through the material again; treating the material with a weak sulphuric acid solution; and removing the acid from the mass.

2. The method of producin cellulosic pulp from vegetable growths of ow lignin content and relatively higher pentosan content comprising the following steps; shredding and cleansin the material; digesting same in water, un er heat, and under a pressure of approximately ten pounds; drawing off the water, heating same and passing it through the material again; treating the material with a weak sulphuric acid solution; and removing the acid from the mass.

' 3. The method of producin cellulosic pulp from vegetable growths o lowlignin content and relatively higher pentosan content com rising the following steps; shredding an cleansing the material; digesting same in approximatel ten times its weight of water and under eat drawing 03 the water, heating same and passinglit through the material again; treating t e material with a weak sulphuric acid solution; and removing the acid'from the mass. v

4. The process of preparin cellulosic' pulp from vegetable growths 0 low ligninacid solution containing substantially 1% of sulphuric acid.

8. The process of producing cellulosic pulp from cornstalks which comprises shredding and comminuting said cornstalks, treating the same under heat and pressure with water, treating said water-treated cornstalks with a 1% solution of sulphuric acid, removing said sulphuric acid, and thereupon treating the cornstalks with water to remove the ,materials solubilized by the said treatment with the sulphuric acid.

In testimony whereof I have fixed my signature.

' ELTON R. DARLING.

hereunto afand relatively high pentosan content which comprises shredding and comminuting the same, removin water-soluble constituents therefrom by lgestion with hot water, and

then hydrolyzing the pentosans therein contained.

5. In the treatment of cellulosic raw materials of the nature of cereal straws such as cornstalks and the like the steps of removing from said materials the water-solu- V ble constituents thereof by means of pressuredigestion with hot water, and then solubilizva ing the pentosanstherein contained.

6. The roce'ss as defined in claim 4, wherein the hy ly'sisis carried out by treatment with a weak'acid solution comprising sulphuric acid.

7. The rocess' as defined in claim 4, where! Q? in the hy lysis is eflected by means of an I