US2040208A - Emulsion for surfacing roads - Google Patents
Emulsion for surfacing roads Download PDFInfo
- Publication number
- US2040208A US2040208A US658471A US65847133A US2040208A US 2040208 A US2040208 A US 2040208A US 658471 A US658471 A US 658471A US 65847133 A US65847133 A US 65847133A US 2040208 A US2040208 A US 2040208A
- Authority
- US
- United States
- Prior art keywords
- tar
- emulsion
- bitumen
- tars
- roads
- 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
- 239000000839 emulsion Substances 0.000 title description 13
- 239000011269 tar Substances 0.000 description 21
- 239000010426 asphalt Substances 0.000 description 14
- 239000000203 mixture Substances 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000004821 distillation Methods 0.000 description 7
- 239000003921 oil Substances 0.000 description 7
- 239000003245 coal Substances 0.000 description 6
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 4
- MWPLVEDNUUSJAV-UHFFFAOYSA-N anthracene Chemical compound C1=CC=CC2=CC3=CC=CC=C3C=C21 MWPLVEDNUUSJAV-UHFFFAOYSA-N 0.000 description 4
- 239000011280 coal tar Substances 0.000 description 4
- 239000010408 film Substances 0.000 description 4
- 239000011287 low-temperature tar Substances 0.000 description 4
- 238000004945 emulsification Methods 0.000 description 3
- 239000003995 emulsifying agent Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000344 soap Substances 0.000 description 3
- 239000004575 stone Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000005018 casein Substances 0.000 description 2
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 2
- 235000021240 caseins Nutrition 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 125000000753 cycloalkyl group Chemical group 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000004525 petroleum distillation Methods 0.000 description 2
- 150000002989 phenols Chemical class 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000001828 Gelatine Substances 0.000 description 1
- 235000008124 Picea excelsa Nutrition 0.000 description 1
- 244000193463 Picea excelsa Species 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000019219 chocolate Nutrition 0.000 description 1
- 239000011300 coal pitch Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000011347 resin Chemical class 0.000 description 1
- 229920005989 resin Chemical class 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000005031 sulfite paper Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
- C08L95/005—Aqueous compositions, e.g. emulsions
Definitions
- This invention relates to emulsions for surfacing roads which at the present time are generally constituted approximately as regards one half by bitumens, that is to say natural bitumens or residues of petroleum distillation and as regards the other'half by water charged with a small proportion of an emulsifying agent such as soap, colloid, gelatine, glue or casein.
- an emulsifying agent such as soap, colloid, gelatine, glue or casein.
- bitumen film is formed as soon as the emulsion comes in contact with the road, and therefore on the surface of the latter, without penetrating into the interior of the ground.
- the new emulsion completely remedies these drawbacks. Its disintegration in fact only commences at the expiration of 10-30 minutes or a longer period if desired, so that it penetrates into the joints of the road stone mosaic before disintegrating or breaking up, thus strengthening the road in a downward direction. A pavement can thus be strengthened, the emulsion getting into the sand of the joint and agglomerating it throughout the whole of its depth.
- this emulsion produces a film which adheres in the broken stones, to sandstone paving blocks and to smooth and polished roads such as those made of compressed asphalt, monolastic, etc.
- This tar must be obtained by distillation of coal carried out in ovens in which the coal is heated gradually and the tars which come out at a temperature between 400 C. and 450 C. with the gas do not come in contact with, or if so only for a short period of time, surfaces heated to a temperature beyond 600 C. which are liable to pyrogenate an excessive proportion of the tar.
- Ovens for distillation called low temperature ovens, the walls of which are at a temperature not exceeding the desired temperature and 2. More particular ovens for the manufacture of lighting gas with continuous charging, among which may be mentioned those of the Clover- West and Woodall-Duckham type, in which the coal descends slowly in vertical cells, gradually reaches a temperature of 400 C. when it gives off its tar which being carried away by the vertically rising gas comes in contact only to a slight extent and for a very short period of time with the walls of the cell and is not pyrogenated.
- This classical coal tar is chiefly constituted by cyclic hydrocarbons, it contains naphthalene and anthracene and a considerable proportion of free carbon and gives on distillation liquid hydrocarbons of a density from 1000 to 1100 when the boiling point of the tar varies from 200 C. to 360 C.
- the low temperature tars considered here contain on the contrary only very little or even no naphthalene and very little anthracene, but on the contrary contain parafiins.
- the liquid hydrocarbons obtained by their distillation have densities from 950 to 1040 when the boiling point of the tar varies from 200 C. to 360 C.
- the pitch remaining at 360 does not resemble the pitch of the normal coal tar, it contains much less free carbon, is richer in volatile matters and is nearer to petroleum bitumen than to ordinary coal pitch. From the point of view of chemical affinities, the oils extracted from these low temperature tars must be classed in the series of the products of petroleum and not in that of cyclic hydrocarbons.
- coal tar to the emulsions hitherto known for the purpose of increasing the surfacing properties, more particularly the plasticity, and for reducing its price.
- the mixing is done in equal proportions or in 40 parts of one and parts of the other.
- the components are liquefied and heated separately to or C. and then mixed together.
- This mixture is much more homogeneous, and the subsequent emulsification is greatly facilitated by adding to the bitumen about 3% of its weight of Swedish residuary oil, which is a well known emulsifying agent for the bituminous emulsions, and which is a by-product obtained in the manufacture of sulphite paper pulp.
- Swedish residuary oil which is a well known emulsifying agent for the bituminous emulsions, and which is a by-product obtained in the manufacture of sulphite paper pulp.
- This is a pure vegetal substance derived from the Pinus Silvestris, consisting mainly in a mixture of fatty acids and resin acids in practically equal quantities, and is entirely free from added mineral mixtures.
- the mixture can also be rendered more homogeneous and the subsequent emulsification facilitated by adding to the bitumen from 2 to 5% of its weight of medium oil, called also phenolic oil, whether partly neutralized or not, this oil being simply the result of distillation of ordinary tars or of low temperature tars and more particularly of these previously referred to in the specification, taking the fraction which passes over between C. and 240 C. It is the part very rich in phenols and homologues.
- This oil to low-temperature tar more particularly if the latter has been partly distilled as subsequently described, also facilitates the homogenization of the mixture and the subsequent emulsification.
- the mixture is emulsified with Water charged with soap, casein and the like in an ordinary apparatus either with a slow mixer or with a disintegrating mill such as a centrifugal turbine constituted by two discs arranged at a distance of about one tenth of a millimeter apart into which the base material and the water charged with the emulsifying agent are introduced in the centre in order to be discharged at the periphery in the form of emulsions produced by the centrifugal force which breaks up the film of the base product into very fine drops which are immediately coated with the soap suds.
- a disintegrating mill such as a centrifugal turbine constituted by two discs arranged at a distance of about one tenth of a millimeter apart into which the base material and the water charged with the emulsifying agent are introduced in the centre in order to be discharged at the periphery in the form of emulsions produced by the centrifugal force which breaks up the film of the base product into very fine drops which are immediately coated with
- a fluid chocolate colour emulsion is thus obtained the spreading of which in a cold state is very easy.
- a mixture containing much less water, up to only 12 to 25% of the total Weight may be prepared in the mixer. This thick mixture must be laid hot, from 45 C. to 80 C. in order to obtain sufficient fluidity. All the relative proportions of low temperature tar and bitumen may be used.
- a stable bituminous emulsion for surfacing of roads consisting of an emulsified mixture of substantially equal parts by weight of a bituminous base and water, said bituminous base being a mixture of substantially equal parts by weight of a low temperature tar obtained by distillation of coal at a temperature between 400 and 450 C. and a bituminous residue of a petroleum distillation, said bituminous base also containing 2 to 5% by weight of a distillation tar fraction rich in phenols and its homologues distilling ofi between 180 and 240 C. and about 3% of Swedish residuary oil.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Road Paving Structures (AREA)
Description
Patented May 12, 1936 UNITED STATES PATENT OFFICE No Drawing.
Application February 24, 1933,
- Serial No. 658,471. In France March 7, 1932 1 Claim. (01. 1341) This invention relates to emulsions for surfacing roads which at the present time are generally constituted approximately as regards one half by bitumens, that is to say natural bitumens or residues of petroleum distillation and as regards the other'half by water charged with a small proportion of an emulsifying agent such as soap, colloid, gelatine, glue or casein.
They usually have the appearance of a dark homogeneous fluid liquid, the solid particles of bitumen in suspension in the water being too fine to be visible to the naked eye.
When laid on the road, these emulsions generally disintegrate in a few minutes, even in five minutes. The solid particles of bitumen join together and agglomerate to a thin film about 1 mm. thick. The water separates and gradually disappears. The bitumen film is formed as soon as the emulsion comes in contact with the road, and therefore on the surface of the latter, without penetrating into the interior of the ground. Moreover the adhesive properties of bitumen are very weak, so that bitumen laid on silex, on paving blocks of sandstone, on smooth roads like certain modern roads (for instance roads of compressed asphalt, of a product called monolastic, and all modern roads made of very fine materials agglomerated with bitumen), does not properly adhere to them and is liable to come off in large slices.
The new emulsion completely remedies these drawbacks. Its disintegration in fact only commences at the expiration of 10-30 minutes or a longer period if desired, so that it penetrates into the joints of the road stone mosaic before disintegrating or breaking up, thus strengthening the road in a downward direction. A pavement can thus be strengthened, the emulsion getting into the sand of the joint and agglomerating it throughout the whole of its depth.
In disintegrating, this emulsion produces a film which adheres in the broken stones, to sandstone paving blocks and to smooth and polished roads such as those made of compressed asphalt, monolastic, etc.
It is chiefly characterized in that in the usual emulsions referred to above about half of the bitumens are replaced by tars of the type called low temperature tars.
This tar must be obtained by distillation of coal carried out in ovens in which the coal is heated gradually and the tars which come out at a temperature between 400 C. and 450 C. with the gas do not come in contact with, or if so only for a short period of time, surfaces heated to a temperature beyond 600 C. which are liable to pyrogenate an excessive proportion of the tar.
These technical conditions are at present fulfilled in the following industrial installations:
1. Ovens for distillation called low temperature ovens, the walls of which are at a temperature not exceeding the desired temperature and 2. More particular ovens for the manufacture of lighting gas with continuous charging, among which may be mentioned those of the Clover- West and Woodall-Duckham type, in which the coal descends slowly in vertical cells, gradually reaches a temperature of 400 C. when it gives off its tar which being carried away by the vertically rising gas comes in contact only to a slight extent and for a very short period of time with the walls of the cell and is not pyrogenated.
It is to be expected that in future many other commercial types of ovens of the same kind will be produced in view 'of the economy of labour obtained with them.
These tars are very different from the coal tars of coke ovens, gas ovens with vertical retorts with intermittent charging or of ovens with horizontal retorts in which the tars, as soon as they leave the coal, meet a wall at 1000 or 1200" C. where they become decomposed and give the classical coal tar. This classical coal tar is chiefly constituted by cyclic hydrocarbons, it contains naphthalene and anthracene and a considerable proportion of free carbon and gives on distillation liquid hydrocarbons of a density from 1000 to 1100 when the boiling point of the tar varies from 200 C. to 360 C. The low temperature tars considered here contain on the contrary only very little or even no naphthalene and very little anthracene, but on the contrary contain parafiins. The liquid hydrocarbons obtained by their distillation have densities from 950 to 1040 when the boiling point of the tar varies from 200 C. to 360 C. The pitch remaining at 360 does not resemble the pitch of the normal coal tar, it contains much less free carbon, is richer in volatile matters and is nearer to petroleum bitumen than to ordinary coal pitch. From the point of view of chemical affinities, the oils extracted from these low temperature tars must be classed in the series of the products of petroleum and not in that of cyclic hydrocarbons.
It has been attempted to add. coal tar to the emulsions hitherto known for the purpose of increasing the surfacing properties, more particularly the plasticity, and for reducing its price.
These attempts failed however for coagulation takes place as soon as the proportion of tar reaches about 20% of the total weight. A granular mass is formed which does not possess any agglomerating power.
On the contrary when part of the bitumen, up to about one half, is replaced according to the invention by low temperature tars, this coagulation need not be feared.
The mixing is done in equal proportions or in 40 parts of one and parts of the other. To make this mixture, the components are liquefied and heated separately to or C. and then mixed together.
This mixture is much more homogeneous, and the subsequent emulsification is greatly facilitated by adding to the bitumen about 3% of its weight of Swedish residuary oil, which is a well known emulsifying agent for the bituminous emulsions, and which is a by-product obtained in the manufacture of sulphite paper pulp. This is a pure vegetal substance derived from the Pinus Silvestris, consisting mainly in a mixture of fatty acids and resin acids in practically equal quantities, and is entirely free from added mineral mixtures.
The mixture can also be rendered more homogeneous and the subsequent emulsification facilitated by adding to the bitumen from 2 to 5% of its weight of medium oil, called also phenolic oil, whether partly neutralized or not, this oil being simply the result of distillation of ordinary tars or of low temperature tars and more particularly of these previously referred to in the specification, taking the fraction which passes over between C. and 240 C. It is the part very rich in phenols and homologues. The addition of this oil to low-temperature tar, more particularly if the latter has been partly distilled as subsequently described, also facilitates the homogenization of the mixture and the subsequent emulsification.
As soon as the tar and bitumen melted at 100 C. are mixed, the mixture is emulsified with Water charged with soap, casein and the like in an ordinary apparatus either with a slow mixer or with a disintegrating mill such as a centrifugal turbine constituted by two discs arranged at a distance of about one tenth of a millimeter apart into which the base material and the water charged with the emulsifying agent are introduced in the centre in order to be discharged at the periphery in the form of emulsions produced by the centrifugal force which breaks up the film of the base product into very fine drops which are immediately coated with the soap suds.
A fluid chocolate colour emulsion is thus obtained the spreading of which in a cold state is very easy.
For special uses which require a surfacing film or skin of great thickness, 5 to 6 cm. for instance, a mixture containing much less water, up to only 12 to 25% of the total Weight, may be prepared in the mixer. This thick mixture must be laid hot, from 45 C. to 80 C. in order to obtain sufficient fluidity. All the relative proportions of low temperature tar and bitumen may be used.-
It has been assumed throughout the preceding description that the low temperature tar was used in the crude state.
This will rarely be the case:
(1) It is advisable to remove the water from the tar.
(2) For applications in depth, it is preferable to remove the volatile parts of the tar which if left in the whole would render it excessively fluid and cause it to penetrate too deeply. This will be the case in new works for penetrating into the stone mosaic of the road and for plugging up surface holes in an old road.
What I claim is:
A stable bituminous emulsion for surfacing of roads, consisting of an emulsified mixture of substantially equal parts by weight of a bituminous base and water, said bituminous base being a mixture of substantially equal parts by weight of a low temperature tar obtained by distillation of coal at a temperature between 400 and 450 C. and a bituminous residue of a petroleum distillation, said bituminous base also containing 2 to 5% by weight of a distillation tar fraction rich in phenols and its homologues distilling ofi between 180 and 240 C. and about 3% of Swedish residuary oil.
ROBERT JOSEPH LACAU.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR2040208X | 1932-03-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2040208A true US2040208A (en) | 1936-05-12 |
Family
ID=9683236
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US658471A Expired - Lifetime US2040208A (en) | 1932-03-07 | 1933-02-24 | Emulsion for surfacing roads |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2040208A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2434243A (en) * | 1942-07-31 | 1948-01-13 | Hjelte Sixten Magnus | Bituminous emulsions |
-
1933
- 1933-02-24 US US658471A patent/US2040208A/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2434243A (en) * | 1942-07-31 | 1948-01-13 | Hjelte Sixten Magnus | Bituminous emulsions |
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