US1372832A - Case-hardening compound and method of manufacturing - Google Patents
Case-hardening compound and method of manufacturing Download PDFInfo
- Publication number
- US1372832A US1372832A US392412A US39241220A US1372832A US 1372832 A US1372832 A US 1372832A US 392412 A US392412 A US 392412A US 39241220 A US39241220 A US 39241220A US 1372832 A US1372832 A US 1372832A
- Authority
- US
- United States
- Prior art keywords
- coal
- compound
- coking
- pitch
- manufacturing
- 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
Links
- 150000001875 compounds Chemical class 0.000 title description 19
- 238000004519 manufacturing process Methods 0.000 title description 7
- 239000000126 substance Substances 0.000 description 21
- 239000003245 coal Substances 0.000 description 19
- 238000004939 coking Methods 0.000 description 17
- 239000000571 coke Substances 0.000 description 12
- 239000000463 material Substances 0.000 description 11
- 239000000203 mixture Substances 0.000 description 9
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 239000002585 base Substances 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 5
- 239000000428 dust Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 4
- 238000012216 screening Methods 0.000 description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 description 4
- 235000017550 sodium carbonate Nutrition 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000011280 coal tar Substances 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000011269 tar Substances 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- HUAUNKAZQWMVFY-UHFFFAOYSA-M sodium;oxocalcium;hydroxide Chemical compound [OH-].[Na+].[Ca]=O HUAUNKAZQWMVFY-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
- C23C8/60—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using solids, e.g. powders, pastes
- C23C8/62—Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using solids, e.g. powders, pastes only one element being applied
- C23C8/64—Carburising
- C23C8/66—Carburising of ferrous surfaces
Definitions
- This invention relates to the art of manufacturing casehardening compounds. It discloses a new material for use in that art and a method of manufacturing a new and improved casehardening compound.
- Another difficulty consists in the actual loss of chemical energizer and the consequent reduction of the efficiency of the material, because of the fixing of the chemicals.
- the ash in chemical combinations which are not For instance, the soda-ash may combine with the siliceous ash of the coal to produce alkali silicates; These are of little or no use as energizers.
- the present invention which consists in the use of the distillates derived from coal as the coking agent in the mixture, instead of the coal itself.
- the ordinary hard fuel pitch instead of other distillates from coal because there aregreat quantities of this material. produced for which under present conditions little or no market exists, this condition having become accentuated with the recent increase in byproduct coke ovens.
- Such pitch is available in abundance with an ash content of less than one per cent. and a fixed carbon content of fifty-five or sixty er cent. when eoked as herein described. his may be compared with the ordinary eight or ten per cent. of ash in coking coal and 'a fixed carbon content of about sixty-five per cent. in the, Pittsburgh coal area.
- T By mixing thev pitch. with the energizing chemicals in any convenient manner, and then coking this mixture, T secure a compound coke which has much greater mechanical strength than the similar product made from coal, and of considerably less weight per unit of volume. quality (low specific density) is of value, as the material is used by bulk, rather than by weight. The casehardening efficiency of the pitch base material is also greater than that This latter parts 0f the coal base material, because of the ab sence' of ash in the pitch.
- dust and fine fragments produced in crushing the compound coke made from pitch may be added to lowing batch of raw materials going to the coking ovens or stills without'reducing the mechanical strength df the coke produced.
- Pitch is the hard, brittle product remaining after the lighter oils and chemicals have been removed from ordinarycoal tar, and is preferable because of its comparativecheapness and high fixed carbon ratio,-but other distillates of coal, as for example the raw tar, may also be used.
- any sort of commercial coking apparatus may be used.
- the chemicals may be mixed with broken up pitch While all the ingredients are solid, then the mixture heated, forming a coked compound, that is'then crushed and screened to size.
- the pitch, or other carbonaceous material may be melted, then the chemicals stirred into the liquid, then the mixture coked, etc.
- the carbonaceous element may be completely coked, crushed and screenech and then the chemicals added and uniformly distributed over the carbo: naceous bases, by some such process as described in U. S. Patent 949446.
- the gases may be either used as fuel for the heating furnace, or may be distilled and reused for other purposes.
- a casehardening compound comprising coked pitch, and an energizing chemical.
- a casehardening compound comprising coked mixture of pitch and an energizing chemical.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Coke Industry (AREA)
Description
edective as energizers.
FATENT HUGH RODMAN, 0F OAKIVLONE, PENNSYLVANIA, ASSIGNOR T9 BUDMAN GHEMICAL COMPANY, OF VERONA, PENNSYLVANIA, A CORPORATION OF PENNSYLVANIA.
CASE-HAEDENING COMPOUND AND METHOD OF MANUFACTURTNG}.
No Drawing.
a specification.
This invention relates to the art of manufacturing casehardening compounds. It discloses a new material for use in that art and a method of manufacturing a new and improved casehardening compound.
it is old to make a casehardening compound by coking a mixture of a coking substance and an energizing chemical so as to produce large masses of compound coke, which are then broken up and sized to meet conunercial requirements. The common practice of this special method consists in mixing ordinary coking coal with soda-ash and lime, all of these ingredients being in dry powdered condition, and then coking this mixture to produce a compound coke containing carbon and the reduced chemicals, this compound coke being subsequently crushed and screened to secure fragments about one-fourth inch in dimension. While a satisfactory casehardening material can be produced by this means, there are several difficulties involved.
One diiiiculty inherent in the use of coal as the coking agent in the method described above consists in the fact that all coals contain considerable ash, or inert material, which may react with the energizing chemicals, or directly with the steel being carbonizcd, to produce glassy adhesions upon the surface of the steel, this reaction being particularly noticeable when soda-ash is used as a chemical energizer.
Another difficulty consists in the actual loss of chemical energizer and the consequent reduction of the efficiency of the material, because of the fixing of the chemicals. by the ash in chemical combinations which are not For instance, the soda-ash may combine with the siliceous ash of the coal to produce alkali silicates; These are of little or no use as energizers.
Another difliculty is that the ordinary sulfur content of coking coal, usually above one per cent. of the weight of the coal, may pass to some extent and under conditions which Specification of Letters Patent. P t mm [W 29 192 Application filed June 28, 1920. Serial No. 392,412.
are not Well understood, into the steel, with the carbon. That is harmful.
Another difliculty consists in the fact that when these large masses of compound coke are crushed there is produced in the crushing operation considerable quantities, generally more than twenty-five per cent. of unmerchan-table fine particles and dust, which must be rejected and lost, orelse worked up by expensive methods into other products. As explained, coal has been used in this special art, subject to the limitations described. It has also been proposed to mix chemical energizers with crude oil and distill to produce a compound coke for casehardening. While this latter proposal has probably not been commercially put into practice, such a method would undoubtedly have some of the same disadvantages that exist along with coal. F or example, the product would have a high ash and sulfur. content, and the difiiculties resulting therefrom would be the same as in the coal compound.
All of these difficulties are overcome by the present invention which consists in the use of the distillates derived from coal as the coking agent in the mixture, instead of the coal itself. Preferably I use the ordinary hard fuel pitch instead of other distillates from coal because there aregreat quantities of this material. produced for which under present conditions little or no market exists, this condition having become accentuated with the recent increase in byproduct coke ovens. Such pitch is available in abundance with an ash content of less than one per cent. and a fixed carbon content of fifty-five or sixty er cent. when eoked as herein described. his may be compared with the ordinary eight or ten per cent. of ash in coking coal and 'a fixed carbon content of about sixty-five per cent. in the, Pittsburgh coal area.
By mixing thev pitch. with the energizing chemicals in any convenient manner, and then coking this mixture, T secure a compound coke which has much greater mechanical strength than the similar product made from coal, and of considerably less weight per unit of volume. quality (low specific density) is of value, as the material is used by bulk, rather than by weight. The casehardening efficiency of the pitch base material is also greater than that This latter parts 0f the coal base material, because of the ab sence' of ash in the pitch.
Furthermore the dust and fine fragments produced in crushing the compound coke made from pitch, may be added to lowing batch of raw materials going to the coking ovens or stills without'reducing the mechanical strength df the coke produced.
In other Words I am able to re-use the unmerchantable fines andv dust by the simple means of recharging them into the still with subsequent raw batches, Without loss of mechanical strength in the 'coke produced; Whereas, if the fines and dust from a coal base compound coke are mixed in With subsequent raw batches, a very weak and unsalable casehardening materialis produced. Thus the chief difficulties inherent in the use of coking coal in this special artmay be overcome by using the cheap (and generally unmarketable) pitch instead of uncoked coking coal.
. Pitch is the hard, brittle product remaining after the lighter oils and chemicals have been removed from ordinarycoal tar, and is preferable because of its comparativecheapness and high fixed carbon ratio,-but other distillates of coal, as for example the raw tar, may also be used.
In the practice of my invention any sort of commercial coking apparatus may be used. The chemicals may be mixed with broken up pitch While all the ingredients are solid, then the mixture heated, forming a coked compound, that is'then crushed and screened to size. Or, the pitch, or other carbonaceous material may be melted, then the chemicals stirred into the liquid, then the mixture coked, etc. Or the carbonaceous element may be completely coked, crushed and screenech and then the chemicals added and uniformly distributed over the carbo: naceous bases, by some such process as described in U. S. Patent 949446. made excellent material each Way, using about seven parts of soda-ash and twelve parts of lime hydrate with one hundred of pitch; and I- have mixed the dust and fines resulting from crushing the comthe fol- I have pound coke so produced With a similar batch of raw materials and produced cokeof apparently the same strength as the first batch.
Other energizing chemicals .may be used.
or at least till the smoke producing distillates have been all given off. The gases may be either used as fuel for the heating furnace, or may be distilled and reused for other purposes.
I claim: 1. A casehardenmg compound comprising coked pitch.
2. A casehardening compound comprising coked pitch, and an energizing chemical.
3. A casehardening compound comprising coked mixture of pitch and an energizing chemical. i
4. The method of manufacturing a casehardeningcompound, comprising mixing energizing chemicals with a coal tar base, coking the mixture, crushing and-screening to size.
5. 'Ihe method of manufacturing a casehardening compound, comprising mixing energizing chemicals with pitch, coking the mixture, crushing and screening to size.
6. The method of manufacturing casehardening materials consisting in coking a coal tar base, crushing and screening it to size, and mixlng suitable energizing chemicals therewith.
7. The method of' manufacturing case hardening materials consisting 1n coking pitch, crushing and screening it to size, and
mixing suitable energizing chemicals therewith.
In testimony whereof I have hereunto set my hand. HUGH RODMAN.
WVitnesses:
Jo. BAILY BROWN, HOWARD S. SNIVELY.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US392412A US1372832A (en) | 1920-06-28 | 1920-06-28 | Case-hardening compound and method of manufacturing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US392412A US1372832A (en) | 1920-06-28 | 1920-06-28 | Case-hardening compound and method of manufacturing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1372832A true US1372832A (en) | 1921-03-29 |
Family
ID=23550475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US392412A Expired - Lifetime US1372832A (en) | 1920-06-28 | 1920-06-28 | Case-hardening compound and method of manufacturing |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1372832A (en) |
-
1920
- 1920-06-28 US US392412A patent/US1372832A/en not_active Expired - Lifetime
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