US111305A - Improvement - Google Patents

Improvement Download PDF

Info

Publication number
US111305A
US111305A US111305DA US111305A US 111305 A US111305 A US 111305A US 111305D A US111305D A US 111305DA US 111305 A US111305 A US 111305A
Authority
US
United States
Prior art keywords
vessel
liquid
crystallizing
pipe
copperas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
Publication date
Application granted granted Critical
Publication of US111305A publication Critical patent/US111305A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/14Sulfates

Definitions

  • Figure l is a transverse section of the apparatus which I employ to carry out my invention, taken on the line c y, Fig. 2.
  • Fig. 2 is a longitudinal section of the same, taken on the line 'v w, Fig. l;
  • Fig. 3 a perspective view of the crystallizing-vessel;
  • Fig'. 4 a perspective view of one ofthe crystallizing-sticks;
  • Fig. 5, a longitudinal section of the blowing apparatus and pipe connected therewitl
  • the same parts are denoted by the same let- .ters in all the figures.
  • This neutralizing-vessel is lined with lead. Its capacity may be about one thousand five hundred gallons, and it is closed except at'the outlet a.
  • the crystallizing-vessel may be lined either with lead or with a composition of one part Trinidad pitch, three parts resin, two parts sulphur, and onepart iron-dust;
  • Frames or slats h h are wedged or otherwise securely adjusted in the vessel F, so a-s to be just on the top of the liquid.
  • An outlet, K is provided for the escape ot uncondensed steam and vapor.4
  • vthe vessel and pipes will be coated with a hard deposit, dilli'cnlt of removal.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

companying drawing,
UNITED STATES PATENT OFFICE.
R. DE WITT BIRCH, OF PHILADELPHIA, PENNSYLVANIA.
Specification forming partei Letters Patent- N0.V11l,305, dated January 3l, 1871.
To all whom it may concern:
Be it known that I, R. DE WITT BIRCH, of the city and county of'Philadelphia, yin the State of Pennsylvania, have invented a neu7 and useful Improvement in the Manufacture of Copperas; l and I do hereby declare the following to lbe a full, clear, and exact description thereof, which will enable others skilled in the art to which it appertains to practice my invention, reference being had to the acwhich forms a part of this specification, and in which;
Figure l is a transverse section of the apparatus which I employ to carry out my invention, taken on the line c y, Fig. 2. Fig. 2 is a longitudinal section of the same, taken on the line 'v w, Fig. l; Fig. 3, a perspective view of the crystallizing-vessel; Fig'. 4, a perspective view of one ofthe crystallizing-sticks; and Fig. 5, a longitudinal section of the blowing apparatus and pipe connected therewitl The same parts are denoted by the same let- .ters in all the figures.
I take the waste liquor from any manufactory where sulphuric acid is employed to act on iron, such as galvanizing works, foundries where castings are cleaned with sulphuric p acid, or other manufaetories, and run this raw liquor into a cistern, where it is allowed to stand for two or three days to deposit impurities, and from which it isv 'pumped into the neutralizing-vessel A. This neutralizing-vessel is lined with lead. Its capacity may be about one thousand five hundred gallons, and it is closed except at'the outlet a. It has also a door, b, through which I throw in enough wrought-iron to neutralize the free acid, and then allow thewholeto stand about four hours, during which it is heated to about S00 Fahrenheit by steam passing through a coil of copper pipe, c, within the neutralizing-vessel. I then run the liquid into the boiler B through the pipe d, (the boiler-end of which is hooked up when not in operation, steam is passed through the copper coil e, and the liquid is thereby boiled down to from 280 to 400 Baume.
The steam and vapors of copperas which escape through the outlets a and b during the operations heretofore described into the chamber C pass over a quantity of common lime in the said chamber, (with which the sulphuric acid unites to form sulphate of lime, depositing metallic iron on the lime,)' and thenceinto the condenser D. By thisv means the greater part of the copperas vapor is intercepted and prevented from passing out into the open air and acting injuriously upon structures and facings of marble or similar stone.
When the liquid has been boiled downto the required density I run it from the boiler into the settling-vessel E by means of the pipe f, which is hooked 'up when not in use, as previously described. After the liquid has stood in the settling-vessel about 4eight hours I run it into the crystallizing-vessel F, elevating the upper end of the pipe g slightly each day, so that it shall always be clear of the previously-deposited sediment.h
The crystallizing-vessel may be lined either with lead or with a composition of one part Trinidad pitch, three parts resin, two parts sulphur, and onepart iron-dust;
Frames or slats h h are wedged or otherwise securely adjusted in the vessel F, so a-s to be just on the top of the liquid. The.ob-
ject of these frames is to keep the crystallizing-sticks (which are thrust between the slats, as shown 1n Fig. 3) immovable and prevent them from floating on the liquid.
I prefer to make the erystallizing-sticks of white l oak. In shape they are octagonal prisms, which. form I have found by experience to be the Vbest adapted to the formation of the crystals on them.
When the crystallizing sticks have been about six days in the crystallizer I remove them and lknock off the crystals of copperas, which are afterward washed in the usual manner, and then laid on the ioor to be dried by the f'ollowin g means: Within the condenser l) is a pipe, G, communicating with the open air, and also with the blowing-machine H, by which a stream of air is forced through .the orilice I. The cold air which enters this pipe is heated by the steam' that escapes from the vessel A and boiler B into the condenser, so that while the steanris condensed and the copperas-vapor prevented, as previously described, from escaping` inany considerable quantity, a current of warm airis continually issuing from the orifice I, in front of which the crystals are laid, and are thereby dried quickly.
An outlet, K, is provided for the escape ot uncondensed steam and vapor.4 The quantity essary to complete the neutralizing process before boiling, thereby incurring loss of time, or
to perform both operations at once, in which case a large quantity of water will be driven oi'before the acid is neutralized, the resulting crystals will contain sulphuric acid, and
vthe vessel and pipes will be coated with a hard deposit, dilli'cnlt of removal.
WhatI claim as my invention, and desire to secure by Letters 'Patent of the United States, is-
1.' The manufacture of' copperas from waste liquor bythe process described.
2.. The process of neutralizing the 'i ree acid in. a separate vessel from that in which the liquid is boiled to the required density.
3. The process of neutralizing, boi-ling,vand' settling the liquid in separate vessels, as described.
4. The above-described method of prevent ing the escape 'of copperas-vapor into the atmosphere.
5. The application of the vapor from the heated liquid to heat the drying-blast, as (lescribed.
6. The combination of the chamber C and condenser D with the pipe G' and blowing- 7. The frames or slats `h h, arranged in the crystallizing vessel, and operating as described.
8. 'llie crystallizing-sticks', made `in the shape and for lthe purpose described.
R, DE WITT BIRCH.
Witnesses;
- WM. R. WRIGHT, THos. A.BURTT.
US111305D Improvement Expired - Lifetime US111305A (en)

Publications (1)

Publication Number Publication Date
US111305A true US111305A (en) 1871-01-31

Family

ID=2180774

Family Applications (1)

Application Number Title Priority Date Filing Date
US111305D Expired - Lifetime US111305A (en) Improvement

Country Status (1)

Country Link
US (1) US111305A (en)

Similar Documents

Publication Publication Date Title
US111305A (en) Improvement
US2221518A (en) Desalting system
DE614877C (en) Process for indirect heating of sulphite liquor
US640026A (en) Process of and apparatus for making copperas.
US843569A (en) Treatment of iron and steel.
US609936A (en) ismay
US461675A (en) Process of and apparatus for refining cotton-seed oil
US41999A (en) Improved apparatus for preventing the loss of sugar during evaporation
US314003A (en) Process of purifying water
US184141A (en) Improvement in processes of preserving wood
US744670A (en) Process of carbonizing material.
US87029A (en) Improved apparatus for redistilling- whiskey and other spirits
US783783A (en) Apparatus for the recovery of volatile acids from solutions.
US72241A (en) Isaac p
US103253A (en) Improvement in apparatus for the production of bromine
US596826A (en) Apparatus for manufacturing calcium acetate
US109546A (en) Improvement in the manufacture of salt
US771629A (en) Apparatus for condensing nitric acid.
US138508A (en) Improvement in turpentine-stills
US166863A (en) Improvement in processes of producing salicylic acid
US77671A (en) Jacob springer
US1104285A (en) Method of heating and evaporating liquids.
US2263A (en) Mode of setting potash-kettles
US101035A (en) Improved apparatus for purifying water for the manufacture of ice
US580274A (en) And heating feed water