US1114045A - Treatment of coal-tar or its products for the removal of the properties therein tending to induce pitch-cancer. - Google Patents
Treatment of coal-tar or its products for the removal of the properties therein tending to induce pitch-cancer. Download PDFInfo
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- US1114045A US1114045A US81799214A US1914817992A US1114045A US 1114045 A US1114045 A US 1114045A US 81799214 A US81799214 A US 81799214A US 1914817992 A US1914817992 A US 1914817992A US 1114045 A US1114045 A US 1114045A
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- tar
- pitch
- cancer
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- 206010028980 Neoplasm Diseases 0.000 title description 17
- 201000011510 cancer Diseases 0.000 title description 17
- 239000011280 coal tar Substances 0.000 title description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 48
- 239000011269 tar Substances 0.000 description 31
- 238000004821 distillation Methods 0.000 description 14
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 14
- 238000000034 method Methods 0.000 description 13
- 239000000126 substance Substances 0.000 description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 8
- 238000002474 experimental method Methods 0.000 description 7
- 239000000295 fuel oil Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- LRFVTYWOQMYALW-UHFFFAOYSA-N 9H-xanthine Chemical compound O=C1NC(=O)NC2=C1NC=N2 LRFVTYWOQMYALW-UHFFFAOYSA-N 0.000 description 2
- IKHGUXGNUITLKF-UHFFFAOYSA-N Acetaldehyde Chemical compound CC=O IKHGUXGNUITLKF-UHFFFAOYSA-N 0.000 description 2
- 239000000061 acid fraction Substances 0.000 description 2
- 229930013930 alkaloid Natural products 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 231100000405 induce cancer Toxicity 0.000 description 2
- 230000001939 inductive effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- OUYCCCASQSFEME-UHFFFAOYSA-N tyrosine Chemical compound OC(=O)C(N)CC1=CC=C(O)C=C1 OUYCCCASQSFEME-UHFFFAOYSA-N 0.000 description 2
- WHRZCXAVMTUTDD-UHFFFAOYSA-N 1h-furo[2,3-d]pyrimidin-2-one Chemical compound N1C(=O)N=C2OC=CC2=C1 WHRZCXAVMTUTDD-UHFFFAOYSA-N 0.000 description 1
- ROHFNLRQFUQHCH-YFKPBYRVSA-N L-leucine Chemical compound CC(C)C[C@H](N)C(O)=O ROHFNLRQFUQHCH-YFKPBYRVSA-N 0.000 description 1
- 235000006173 Larrea tridentata Nutrition 0.000 description 1
- 244000073231 Larrea tridentata Species 0.000 description 1
- ROHFNLRQFUQHCH-UHFFFAOYSA-N Leucine Natural products CC(C)CC(N)C(O)=O ROHFNLRQFUQHCH-UHFFFAOYSA-N 0.000 description 1
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000005167 amoeboid movement Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000601 blood cell Anatomy 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- CVSVTCORWBXHQV-UHFFFAOYSA-N creatine Chemical compound NC(=[NH2+])N(C)CC([O-])=O CVSVTCORWBXHQV-UHFFFAOYSA-N 0.000 description 1
- 229960002126 creosote Drugs 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 150000002897 organic nitrogen compounds Chemical class 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G21/00—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents
- C10G21/06—Refining of hydrocarbon oils, in the absence of hydrogen, by extraction with selective solvents characterised by the solvent used
Definitions
- auxetlcsand kinetics were present, these being known under the-names of auxetlcsand kinetics respectively. Either of thesealone will not induce cancer, but when .both. are present cancer may be induced in workers who are constantly working in the presence of dust containing the substances.
- the auxetics are certain agents present in dead matter, and are exc'iters of reproduction which stimulate cell-multiplication; among them may be mentioned creatin, xanthin (which contain the amidin grouping N-Q-N) methylamin (a primary amin) leucin and tyrosin (amino-acids).
- the kinetics are alkaloids which excite amoeboid movements in the blood cells. Most alkaloids have this property.
- para-formalde-' hyde, or otheraldehydes maybe used, as-it 18 found that the action in question is due to the-presence of an aldehyde, andpraetically all aldehydes act, to some extent at least, to get rid of auxetics.
- acetic aldehyde may be used, or other aldehydes of the -fatty,group.
- the amount of the aldehyde added and thestage in the process at which .it is added, will vary according to particular requirements and t0 the condition of the tar or pitch to be treated.
- Figure 1 shows a portion of the apparatus
- Figs. 2 and 3 are detail views of a mixing jet used therein.
- the steam is introduced into the still a (only part of which is shown) through a pipe I) from a boiler capable of supplying steam at the required pressure.
- Commercial formalin is pumped through apipe d into storage vessels 0 under a suitable air pressure, such as 20 to 30 pounds per square inch, and is supplied from these vessels as required through cocks h and a pipe 0 to a jet for mixing it with the steam.
- a suitable form of jet is shown in Fig. 2 in elevation, partly in section, and in Fig. 3 in plan.
- the pipe e terminates in a fitting at the top of the device and communicates with a jet 9 in a glass sight tube f. The lower end of this tube communicates with the steam pipe b near to its point of entry into the still a.
- the feed of the formalin can be observed and the jet can be removed and replaced easily if it becomes choked, while the feed of the formalin can be regulated by the cocks h as required.
- the regulation can be effected also by varying the pressure in the vessels 0, the size of the orifice of the nozzle g, the strength of the solution, or by any combination 'of these means.
- the formalin is introduced into the compartments of the still where the heavy oil fractions are i being distilled'at temperatures above 250 0., and if jets are used as above described, the feed of formalin may be continuous in these compartments.
- the pitch drawn oft from the last compartment will be found to be substantially free from auxetics, so that it would have little or no tendency to induce cancer among operatives working with it.
- the invention is not limited to the particular ways of adding the formaldehyde or its equivalent as set forth above, but any suitable method may be adopted of adding it at any convenient stage in the distillation or to the pitch residue after the completion ofthe distillation.
- a process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer the process consisting in mixing with the tar or pitch less than 1% of a substance yielding an aldehyde.
- a process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer the process consisting in mixing with the tar or pitch less than 1% of a substance containing and yielding an aldehyde.
- a process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer consisting in adding less than 1% of an aldehyde to the tar or pitch before the completion of the distillation.
- a process for treating tar or pitch with the object of removing therefrom the propertiestending to induce pitch cancer consisting in adding less than 1% of formalin to the tar .or pitch before the completion of the distillation.
- a process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer consisting in adding less than 1% of a substance yielding an aldehyde to the tar during the distillation thereof at a stage after the separation of the carbolic acid fraction and before the separation of the heavy oil fraction.
- a process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer consisting in adding less than 1% of a substance yielding an aldehyde to the tar during the distillation thereof at a stage after the separation of the carbolic acid fraction vand before the separation of the heavy oil fraction, and adding to the residue'a further quantity of said substance after the completion of the distillation.
- A'process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer consisting in mixing a small amount of formalin with steam and spraying the mixture into thedistillation still after the carbolicacid fraction has been separated and before the heavy oil fraction is separated.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Description
Y H. w; ROBINSON. TREATMENT OF GOAL TAR OR ITS PRODUOTS FOR THE REMOVAL. OF THE PROPERTIES THEREIN PENDING TO INDUCE PITCH CANCER.
APPLICATION FILED FEB.11. 1914. I 1,1 14,045,. Patented Oct. 20, 1914.
UNITED STATES PATENT OFFICE.
HERBERT W. ROBINSON, OF SEDGLEY, ENGLAND.
TREATMENT OF COAL-TAR OR ITS PRODUCTS FOR THE REMOVAL OF THE PROPERTIES TEEREIN TENDINGTO INDUCE PITCH-CANCER.
Specification of Letters Patent.
Patented Oct. 20, 1914.
Application filed February 11, 1914. Serial N 0. 817,992.
Ta all whom it may concern Be it known that I, HERBERT WILLIAM ROBINSON, a subject of the King of Great Britain, and resident of Turls Hill House, Sedgley, in the county of Stafford, England, have invented certain new and useful Improvements Relating to the Treatment of Coal-Tar or Its Products forthe Removal of the Properties Therein Tending to Induce Pitch-Cancer, of which the following is a specification. 7
Recent experiments-have been directed to the problem of ascertaining thecauses of cancer among workers in the industries producing and using'pitch, and particularly in the manufacture of briquets wherein the pitch is employed as a binding agent for the coal dust. A recent publication on this subject T he Problem of the Gas lVOrZcs Pitch Industries and Cancer issued under the auspices of the John Howard McFadden researches (John Murray, Albemarle Street,
London, W. 1912) gives particulars of researches showing what results have been ob-I tained in experiments withsamples of'pitch and oils obtained from coal tar; these experiments showedthat cancer would only be, induced when two diiterent classes, of sub;
stances were present, these being known under the-names of auxetlcsand kinetics respectively. Either of thesealone will not induce cancer, but when .both. are present cancer may be induced in workers who are constantly working in the presence of dust containing the substances. The auxetics are certain agents present in dead matter, and are exc'iters of reproduction which stimulate cell-multiplication; among them may be mentioned creatin, xanthin (which contain the amidin grouping N-Q-N) methylamin (a primary amin) leucin and tyrosin (amino-acids). The kinetics are alkaloids which excite amoeboid movements in the blood cells. Most alkaloids have this property.
Various ways were suggested of treating either the pitch or the tar in order to remove from it either the auxetics or' the kinetics, and so to render it 1nnocuous in so far as the inducing of pitch cancer was concerned. It was suggested for instance that the desired result could be obtained by mixing a considerable amount of water with the tar when the water would dissolve out some of the constituents of the tar. The aqueous solution was then to be separated from the tar by centrifugal action or, otherwise. Experiments onthe resulting pitch and oils showed that the kinetics could be removed 1n this way, and usually also the auxetics.
Now this process is not a practicable one, for
the present at any rate, from the point of view of the tar distiller. The expense is too great and valuable constituents of the tar are dissolved out by the water. I have therefore made some experiments with the opject of ascertaining whether the addition 0 some chemical substance to the-tar would produce the desired result at a comparetively small expense, and without deleteriously affecting the value ofthe tar and of the products obtained therefrom. In so far as these experiments have been carried u to thepresent, it has been found that an a dition of even small quantities of formaldehyde to the'tar at a convenient stagejin the distillation process, Iproduces at'least beneficial results, the pitch obtained being free from auxetics, or containing only small traces so that it would be com aratively harmless in so far as the risk 0' inducing cancer is concerned. The action of the formaldehyde is doubtless due to its property of condensln'g organic nitrogen compounds, these being the compounds in the tar which by theresearch above referred to, are shown to'have auxetic properties.
In place of formaldehyde, para-formalde-' hyde, or otheraldehydes maybe used, as-it 18 found that the action in question is due to the-presence of an aldehyde, andpraetically all aldehydes act, to some extent at least, to get rid of auxetics. 'For example, acetic aldehyde may be used, or other aldehydes of the -fatty,group. The amount of the aldehyde added and thestage in the process at which .it is added, will vary according to particular requirements and t0 the condition of the tar or pitch to be treated. It is not essential for most purposes to add the aldehyde in a pure form, and substances containing a suitable aldehyde or ca able of yielding an aldehyde during the su' sequent treatment of theproduct, may be added to the tar of pitch. For example, sugar decomposes at a temperature below 250 C., with the formation of vformaldehyde, and for somepurposes it may be cheaper or better to add sugar or the like 'to the product before or during the heating process in order to insure the presence of suflicient aldehyde to render the resulting pitch substantially free from auxetics.
When formaldehyde is to be added to the tar during the distillation, it is generally most convenient to efiect the distillation in the ordinary Way until the carbolic acid and the earlier creosote fractions have been taken off. When the temperature of the residue in the still reaches about 250 to 270 (1., the distillation of further fractions consisting of heavy oils and so forth, is assisted by a current of steam introduced for example through a perforated pipe in the still, and the formaldehyde may be introduced conveniently with this steam. I Alternatively, the temperature of the material in the still may be reduced if necessary, and the formaldehyde or a substance capable of yielding a suitable aldehyde may be simply added before heating further to continue the distillation. When the formaldehyde .is-
added with steam, the means for effecting the addition may be as shown in the accompanying drawing.
In this, Figure 1 shows a portion of the apparatus, and Figs. 2 and 3 are detail views of a mixing jet used therein.
The steam is introduced into the still a (only part of which is shown) through a pipe I) from a boiler capable of supplying steam at the required pressure. Commercial formalin is pumped through apipe d into storage vessels 0 under a suitable air pressure, such as 20 to 30 pounds per square inch, and is supplied from these vessels as required through cocks h and a pipe 0 to a jet for mixing it with the steam. A suitable form of jet is shown in Fig. 2 in elevation, partly in section, and in Fig. 3 in plan. The pipe e terminates in a fitting at the top of the device and communicates with a jet 9 in a glass sight tube f. The lower end of this tube communicates with the steam pipe b near to its point of entry into the still a.
,With this construction, the feed of the formalin can be observed and the jet can be removed and replaced easily if it becomes choked, while the feed of the formalin can be regulated by the cocks h as required. The regulation can be effected also by varying the pressure in the vessels 0, the size of the orifice of the nozzle g, the strength of the solution, or by any combination 'of these means. In the case of intermittent stills which are com letely emptied after each distillation of a c large of tar, it has been found convenient to introduce about two-thirds of the total charge of formalin for each charge of tar, during the distillation as set forth above, and to add the remaining 0ne-third after the withdrawal of the fire and while the Pitch residue is cooling in the still. About one anda half gallons of commercial formalin (40% solution of formaldehyde) have been used in successful experiments for a charge of 2,000 gallons of tar, but the quantity can be varied to any extent according to the condition of the tar and the results shown by experiment. The object is to eliminate the auxetics as far as possible from the product, and to do this with the least expenditure of formalin or its equivalent.
.In the case of continuous stills, the formalin is introduced into the compartments of the still where the heavy oil fractions are i being distilled'at temperatures above 250 0., and if jets are used as above described, the feed of formalin may be continuous in these compartments. The pitch drawn oft from the last compartment will be found to be substantially free from auxetics, so that it would have little or no tendency to induce cancer among operatives working with it.
The invention is not limited to the particular ways of adding the formaldehyde or its equivalent as set forth above, but any suitable method may be adopted of adding it at any convenient stage in the distillation or to the pitch residue after the completion ofthe distillation.
Having thus described my invention, what I claim as new and desire to secure by Letters Patent is:-
1. A process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer, the process consisting in mixing with the tar or pitch less than 1% of a substance yielding an aldehyde.
2. A process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer, the process consisting in mixing with the tar or pitch less than 1% of a substance containing and yielding an aldehyde.
3. A process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer, consisting in adding less than 1% of an aldehyde to the tar or pitch before the completion of the distillation.
4. A process for treating tar or pitch with the object of removing therefrom the propertiestending to induce pitch cancer, consisting in adding less than 1% of formalin to the tar .or pitch before the completion of the distillation.
5. A process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer, consisting in adding less than 1% of a substance yielding an aldehyde to the tar during the distillation thereof at a stage after the separation of the carbolic acid fraction and before the separation of the heavy oil fraction.
6. A process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer, consisting in adding less than 1% of a substance yielding an aldehyde to the tar during the distillation thereof at a stage after the separation of the carbolic acid fraction vand before the separation of the heavy oil fraction, and adding to the residue'a further quantity of said substance after the completion of the distillation.
' 7. A'process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer, consisting in mixing a small amount of formalin with steam and spraying the mixture into thedistillation still after the carbolicacid fraction has been separated and before the heavy oil fraction is separated.
'8. A process for treating tar or pitch with the object of removing therefrom the properties tending to induce pitch cancer,'consisting in spraying a small amount of formalin under pressure into steam, and supplying the mixture of steam and formalin into the presence of two subscribing witnesses.
- HERBERT W. ROBINSON.
Witnesses:
HUBERT A. GILL, H. W. BLAKE.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US81799214A US1114045A (en) | 1914-02-11 | 1914-02-11 | Treatment of coal-tar or its products for the removal of the properties therein tending to induce pitch-cancer. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US81799214A US1114045A (en) | 1914-02-11 | 1914-02-11 | Treatment of coal-tar or its products for the removal of the properties therein tending to induce pitch-cancer. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1114045A true US1114045A (en) | 1914-10-20 |
Family
ID=3182228
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US81799214A Expired - Lifetime US1114045A (en) | 1914-02-11 | 1914-02-11 | Treatment of coal-tar or its products for the removal of the properties therein tending to induce pitch-cancer. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1114045A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2848379A (en) * | 1953-07-16 | 1958-08-19 | Exxon Research Engineering Co | Treatment of high boiling catalytically cracked products with activated carbon |
| US2862867A (en) * | 1953-06-17 | 1958-12-02 | Exxon Research Engineering Co | Reduction of carcinogenicity of high boiling catalytically cracked oil by partial oxidation |
-
1914
- 1914-02-11 US US81799214A patent/US1114045A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2862867A (en) * | 1953-06-17 | 1958-12-02 | Exxon Research Engineering Co | Reduction of carcinogenicity of high boiling catalytically cracked oil by partial oxidation |
| US2848379A (en) * | 1953-07-16 | 1958-08-19 | Exxon Research Engineering Co | Treatment of high boiling catalytically cracked products with activated carbon |
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