US775028A - Apparatus for preparing fiber for paper-making. - Google Patents

Apparatus for preparing fiber for paper-making. Download PDF

Info

Publication number
US775028A
US775028A US21691904A US1904216919A US775028A US 775028 A US775028 A US 775028A US 21691904 A US21691904 A US 21691904A US 1904216919 A US1904216919 A US 1904216919A US 775028 A US775028 A US 775028A
Authority
US
United States
Prior art keywords
digester
absorber
pipe
gas
condenser
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
US21691904A
Inventor
Frank H Cloudman
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
US case filed in Florida Middle District Court litigation Critical https://portal.unifiedpatents.com/litigation/Florida%20Middle%20District%20Court/case/8%3A18-cv-00264 Source: District Court Jurisdiction: Florida Middle District Court "Unified Patents Litigation Data" by Unified Patents is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Individual filed Critical Individual
Priority to US21691904A priority Critical patent/US775028A/en
Application granted granted Critical
Publication of US775028A publication Critical patent/US775028A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00Regeneration of pulp liquors or effluent waste waters
    • D21C11/06Treatment of pulp gases; Recovery of the heat content of the gases; Treatment of gases arising from various sources in pulp and paper mills; Regeneration of gaseous SO2, e.g. arising from liquors containing sulfur compounds

Definitions

  • My invention is an improvement on the bisulfite method, and has for its principal object the saving of sulfur or sulfur products used in this process.
  • the usual method of procedure in the'manui'acture of fiber by this process is to fill a large vessel,'called a digester, with wood in the form of chips and then run in the required amount of bisulfite-of-lime solution, close up tightly,- and apply steam by means of proper pipes at the bottom of the digester. As the temperature of the solution rises some of the sulfur in the form of sulfur dioxid or gas is driven off and, together with the air contained in the wood and steam from the heated liquid, rises to the top of the digester.
  • the object of my invention is to recover the gas and return it back into the digester.
  • the digester is shown at A.
  • the relief-pipe D for the gas leads from the top of the digester to an absorber C, which is arranged at some distance above the top of the digester and is filled with limestone or other suitable material.
  • the separator or condenser E which may be'of ordinary form having a series of vertical pipes (6 extending through a water-space Z) of the chamber, with which water-space the water-inlet and water-outlet pipes 0 (Z connect.
  • This condenser chamber has a partition extending across it near its upper end, and the series of pipes open upwardly through this partition, and an air valve or cook E, connected with the space above this partition, is adapted to discharge any air which may separate from the gas.
  • the absorber is connected at its lower end by a return-pipe E with the lower end of the digester, and a check-valve is located at G in the said pipe,which closes toward the absorber to prevent the pressure of gas in the digester from passing back through this pipe to the absorber.
  • the pipe for introducing steam to the bottom of the digester is shown at L and the blowpipe at M.
  • a valve is also provided in the relief-pipe at K.
  • the approximate liq uid-level in the digester is indicated at H, while the'approximate liquid-level in the return-pipe E is indicated at I.
  • the operation is as follows:
  • the digester A is filled with wood in the form of chips and the proper amount of bisuliite-of-lime solution is run in with the chips. Steam is then applied in the usual manner at the bottom of the digester.
  • the accumulation v of gas and air can be watched, and when deemed necessary the valve K in the reliefpipe can be opened and the gas, air, and steam allowed to pass up through pipe D to the absorber (J, and here the gas will be absorbed by the limestone or other suitable absorbent material, and absorption of the gas will also take place by the water of condensation resulting from the action of the condenser, and when a sufficient height of water of condensation, with its contained gas, has been reached in the return-pipe it will be forced into the digester by gravity, it being observed that the condenser and absorber are located at a considerable distance above theztop of the digester, and the pressure being equalized throughout the system
  • an absorber arranged at a higher level, a relief-pipe from the digester to the absorber, a condenser arranged above and connected With the absorber and a return-pipe from the absorber to the bottom of the cligcster, substantially as described.
  • a digester' In combination, a digester', an absorber arranged at a higher level and connected with the top of the digester, a condenser connected with the absorber and arranged above the same, a return-pipe to the digester and an airrelief pipe at the top of the condenser.
  • a digester In combination, a digester, an absorber, a pipe leading from the digester to the absorber, a valve in said pipe, a condenser arranged above and connected with the digester, a return-pipe from the absorber to the digester and a check-valve in the said pipe, substantially as described.

Description

No. 775,028. PATENTED NOV 15, 1904.
' P. H. OLDUDMAN.
APPARATUS FOR PREPARING FIBER FOR PAPER MAKING.
, APPLICATION FILED JULY 15, 1904.
no MODEL.
G I AIRVALVPL ..A PPROXIMA r: Llqum LE vs 1.
I I A awwewboz I vi em 0 G RANK CLOUDMAN 2%? )%fh mm,%md om Weiam UNITED STATES Patented November 15, 1904.
PATENT OFFICE.
FRANK H. CLOUDMAN, OF VVESTBROOK, MAINE.
SPECIFICATION forming part of Letters Patent No. 775,028, dated November 15, 1904. Application filed July 15, 1904. Serial No. 216,919. (No model.)
To all whom, it may concern.-
Be it known that I, FRANK H. GLOUDMAN, a citizen of the United States, residing at Westbrook, Cumberland county, Maine, (whose post-office address is FRANK H. CLoUDMAN, \Vestbrook, Cumberland county, State of Maine) have invented certain new and useful Improvements in Apparatus for Preparing Fiber for PaperNIaking, of which the following is a specification.
My invention is an improvement on the bisulfite method, and has for its principal object the saving of sulfur or sulfur products used in this process. The usual method of procedure in the'manui'acture of fiber by this process is to fill a large vessel,'called a digester, with wood in the form of chips and then run in the required amount of bisulfite-of-lime solution, close up tightly,- and apply steam by means of proper pipes at the bottom of the digester. As the temperature of the solution rises some of the sulfur in the form of sulfur dioxid or gas is driven off and, together with the air contained in the wood and steam from the heated liquid, rises to the top of the digester. This accumulation of gas and air if allowed to remain would prevent the proper action of the solutions upon the wood, and therefore the usual custom is to relieve or allow a quantity of these gases to escape by means of proper pipes and valves leading from the top of the digester, more or less steam necessarily escaping at the same time.
The object of my invention is to recover the gas and return it back into the digester.
In the accompanying drawing the apparatus is shown in central vertical section.
The digester is shown at A. The relief-pipe D for the gas leads from the top of the digester to an absorber C, which is arranged at some distance above the top of the digester and is filled with limestone or other suitable material. Above this absorber is located the separator or condenser E, which may be'of ordinary form having a series of vertical pipes (6 extending through a water-space Z) of the chamber, with which water-space the water-inlet and water-outlet pipes 0 (Z connect. This condenser chamber has a partition extending across it near its upper end, and the series of pipes open upwardly through this partition, and an air valve or cook E, connected with the space above this partition, is adapted to discharge any air which may separate from the gas. The absorber is connected at its lower end by a return-pipe E with the lower end of the digester, and a check-valve is located at G in the said pipe,which closes toward the absorber to prevent the pressure of gas in the digester from passing back through this pipe to the absorber.
The pipe for introducing steam to the bottom of the digester is shown at L and the blowpipe at M. A valve is also provided in the relief-pipe at K. The approximate liq uid-level in the digester is indicated at H, while the'approximate liquid-level in the return-pipe E is indicated at I.
The operation 'is as follows: The digester A is filled with wood in the form of chips and the proper amount of bisuliite-of-lime solution is run in with the chips. Steam is then applied in the usual manner at the bottom of the digester. By means of gages and ther mometers (not shown, but suitably connected to the top of the digester) the accumulation v of gas and air can be watched, and when deemed necessary the valve K in the reliefpipe can be opened and the gas, air, and steam allowed to pass up through pipe D to the absorber (J, and here the gas will be absorbed by the limestone or other suitable absorbent material, and absorption of the gas will also take place by the water of condensation resulting from the action of the condenser, and when a sufficient height of water of condensation, with its contained gas, has been reached in the return-pipe it will be forced into the digester by gravity, it being observed that the condenser and absorber are located at a considerable distance above theztop of the digester, and the pressure being equalized throughout the system when the valve K is opened the return of the liquid will take place by gravity. The air-relief valve F, it will be noticed, is at the highest point in the system, and this may be of the automatic or hand opcrating type. T
It will be observed also that the gas and steam passing out from the digester flows first into the absorber, where the gas is acted on by the absorbing material and the descending fluid from the condenser.
I claim as my invention,
1. In combination with a digester, a gas absorber and condenser, pipes connecting said absorber and condenser with the upper and lower parts of the digester, and valve means whereby the pressure may be equalized, the said absorber and condenser being arranged above the level of the digester whereby the return of the gas and liquid takes place by gravity, substantially as described.
2. In combination with a digester, an absorber arranged at a higher level, a relief-pipe from the digester to the absorber, a condenser arranged above and connected With the absorber and a return-pipe from the absorber to the bottom of the cligcster, substantially as described.
3. In combination, a digester', an absorber arranged at a higher level and connected with the top of the digester, a condenser connected with the absorber and arranged above the same, a return-pipe to the digester and an airrelief pipe at the top of the condenser.
4. In combination, a digester, an absorber, a pipe leading from the digester to the absorber, a valve in said pipe, a condenser arranged above and connected with the digester, a return-pipe from the absorber to the digester and a check-valve in the said pipe, substantially as described.
In testimony whereof I aifix my signature in presence of two witnesses.
FRANK H. CLOUDMAN.
Witnesses:
A. E. GIBBS, EMMoNs BRYANT.
US21691904A 1904-07-15 1904-07-15 Apparatus for preparing fiber for paper-making. Expired - Lifetime US775028A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US21691904A US775028A (en) 1904-07-15 1904-07-15 Apparatus for preparing fiber for paper-making.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US21691904A US775028A (en) 1904-07-15 1904-07-15 Apparatus for preparing fiber for paper-making.

Publications (1)

Publication Number Publication Date
US775028A true US775028A (en) 1904-11-15

Family

ID=2843513

Family Applications (1)

Application Number Title Priority Date Filing Date
US21691904A Expired - Lifetime US775028A (en) 1904-07-15 1904-07-15 Apparatus for preparing fiber for paper-making.

Country Status (1)

Country Link
US (1) US775028A (en)

Similar Documents

Publication Publication Date Title
US775028A (en) Apparatus for preparing fiber for paper-making.
US775027A (en) Apparatus for preparing fiber for paper-making purposes.
US2205374A (en) Digesting process and apparatus
US1552071A (en) Deaerating apparatus
US759660A (en) Apparatus for feeding water to steam-boilers.
US127197A (en) Improvement in vacuum-stills
US499403A (en) E morris petebg co
US2023630A (en) Feed water degassing apparatus
US1661140A (en) Process of sterilizing vegetable products
US724051A (en) Apparatus for raising liquids.
US775450A (en) Vomiting-keir.
US1601478A (en) Steam pump or boiler feeder
US1862243A (en) Apparatus for recovering acid and heat units thereof from digesters and for preparing digester liquor
US1076078A (en) Reclaiming system in a sulfite pulp process.
US727499A (en) Steam-boiler.
US357371A (en) Process of and apparatus for cooking wood pulp
US100196A (en) Separator to be used in distelling liques
US938573A (en) Feed-water heater.
US1645132A (en) Deaerating water
US1866091A (en) Apparatus for treating liquids
US168382A (en) Improvement in apparatus for the manufacture of paper-pulp
US53298A (en) Improved process for evaporating alkaline solutions
US1504618A (en) Apparatus for water deaeration
US541686A (en) Defecator
US1847691A (en) Apparatus for conducting steam from an economizer to alpha boiler