US2731457A - Production and use of a urea suspension - Google Patents
Production and use of a urea suspension Download PDFInfo
- Publication number
- US2731457A US2731457A US22655751A US2731457A US 2731457 A US2731457 A US 2731457A US 22655751 A US22655751 A US 22655751A US 2731457 A US2731457 A US 2731457A
- Authority
- US
- United States
- Prior art keywords
- urea
- oil
- hydrocarbon
- petroleum
- suspension
- 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
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 title description 77
- 239000004202 carbamide Substances 0.000 title description 77
- 238000004519 manufacturing process Methods 0.000 title description 13
- 239000000725 suspension Substances 0.000 title description 12
- 235000013877 carbamide Nutrition 0.000 description 77
- 239000003921 oil Substances 0.000 description 41
- 229930195733 hydrocarbon Natural products 0.000 description 31
- 150000002430 hydrocarbons Chemical class 0.000 description 30
- 239000004215 Carbon black (E152) Substances 0.000 description 27
- 239000003208 petroleum Substances 0.000 description 24
- 239000000839 emulsion Substances 0.000 description 18
- 238000000034 method Methods 0.000 description 16
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 13
- 239000003085 diluting agent Substances 0.000 description 12
- 239000007788 liquid Substances 0.000 description 11
- 238000004821 distillation Methods 0.000 description 8
- 239000012053 oil suspension Substances 0.000 description 8
- 150000003672 ureas Chemical class 0.000 description 8
- 239000000203 mixture Substances 0.000 description 7
- 239000012071 phase Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000001816 cooling Methods 0.000 description 6
- 230000035939 shock Effects 0.000 description 6
- 239000003795 chemical substances by application Substances 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 239000000446 fuel Substances 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- 239000013078 crystal Substances 0.000 description 2
- 238000004508 fractional distillation Methods 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- QOTAEASRCGCJDN-UHFFFAOYSA-N [C].CO Chemical compound [C].CO QOTAEASRCGCJDN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C273/00—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups
- C07C273/02—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds
-
- 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
- C10G31/00—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for
- C10G31/06—Refining of hydrocarbon oils, in the absence of hydrogen, by methods not otherwise provided for by heating, cooling, or pressure treatment
Definitions
- a mixture of methanol and hydrocanbondiluent is removed overheadi fromfractionator 13 by line.1.6", through cooler'1'7 and line 18 and is recycled to the reactor; 1 by line. 4:
- a mixture of urea-inactive components of: the feedstock together with hydrocarbon diluent is removed. from filter 6' by lines-19 and constitutes-:- thefinishedfuei; Liquidurea; is removed from the sepa-- ratorglo tby 1ine:20;an,d-is. passed to an. emulsifier 21 fed with hot-.fcedzoil. by line: 222from heater 28.
- the emulsified-rurea/oil mixture is removed by line.- 23.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB12287/50A GB714327A (en) | 1950-05-17 | 1950-05-17 | Improvements in or relating to the production of urea in finely divided form and to the refining of petroleum by means of urea in finely divided form |
Publications (1)
Publication Number | Publication Date |
---|---|
US2731457A true US2731457A (en) | 1956-01-17 |
Family
ID=10001784
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US22655751 Expired - Lifetime US2731457A (en) | 1950-05-17 | 1951-05-16 | Production and use of a urea suspension |
Country Status (4)
Country | Link |
---|---|
US (1) | US2731457A (d) |
BE (1) | BE503277A (d) |
GB (1) | GB714327A (d) |
NL (1) | NL75904C (d) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2911350A (en) * | 1959-11-03 | Production of low cold-test oils by |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1049032B (de) * | 1955-04-29 | 1959-01-22 | Oelwerke Julius Schindler G M | Verfahren zum kontinuierlichen Entparaffinieren von Kohlenwasserstoffoelen mittels Harnstoffaddukten |
IT1096661B (it) * | 1978-06-13 | 1985-08-26 | Montedison Spa | Procedimento per la preparazione di prodotti in forma sferoidale solidi a temperatura ambiente |
US6725651B2 (en) | 2000-11-16 | 2004-04-27 | Toyota Jidosha Kabushiki Kaisha | Reducing agent for emission control system, reducing-agent supply device, and emission control system using the reducing agent |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1558619A (en) * | 1921-02-05 | 1925-10-27 | Sharples Specialty Co | Method and apparatus for avoiding shock chill in precipitating substances from liquids |
US2031117A (en) * | 1932-10-24 | 1936-02-18 | Union Oil Co | Process for dewaxing oil |
US2499820A (en) * | 1947-02-21 | 1950-03-07 | Thiourea-hydrocarbon complexes | |
FR959374A (d) * | 1947-01-07 | 1950-03-28 | ||
US2606140A (en) * | 1948-12-30 | 1952-08-05 | Texas Co | Separation of wax constituents and the like from oil |
-
1950
- 1950-05-17 GB GB12287/50A patent/GB714327A/en not_active Expired
-
1951
- 1951-05-10 NL NL161132A patent/NL75904C/xx active
- 1951-05-16 US US22655751 patent/US2731457A/en not_active Expired - Lifetime
- 1951-05-16 BE BE503277D patent/BE503277A/xx unknown
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1558619A (en) * | 1921-02-05 | 1925-10-27 | Sharples Specialty Co | Method and apparatus for avoiding shock chill in precipitating substances from liquids |
US2031117A (en) * | 1932-10-24 | 1936-02-18 | Union Oil Co | Process for dewaxing oil |
FR959374A (d) * | 1947-01-07 | 1950-03-28 | ||
US2499820A (en) * | 1947-02-21 | 1950-03-07 | Thiourea-hydrocarbon complexes | |
US2606140A (en) * | 1948-12-30 | 1952-08-05 | Texas Co | Separation of wax constituents and the like from oil |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2911350A (en) * | 1959-11-03 | Production of low cold-test oils by |
Also Published As
Publication number | Publication date |
---|---|
NL75904C (d) | 1954-09-15 |
GB714327A (en) | 1954-08-25 |
BE503277A (d) | 1951-06-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2355366A (en) | Process for catalytically desulphurizing hydrocarbon oil | |
US2847306A (en) | Process for recovery of oil from shale | |
US3179584A (en) | Oil coking with increased hydrogen production | |
GB913730A (en) | Desulfurization of hydrocarbon oils | |
US2692226A (en) | Shale oil refining process | |
US2282451A (en) | Desulphurizing and cracking process | |
US2966450A (en) | Shale oil refining process using a selective solvent and anhydrous hydrogen chloride | |
US2731457A (en) | Production and use of a urea suspension | |
US2331429A (en) | Isomerization of hydrocarbons | |
US2847362A (en) | Two-stage treating process | |
US1881534A (en) | Process of refining hydrocarbon oils | |
US2642466A (en) | Production of olefinic hydrocarbons | |
US2653176A (en) | Production of aromatics from petroleum | |
US2951886A (en) | Recovery and purification of benzene | |
US2427009A (en) | Catalytic cracking of hydrocarbons in the presence of hydrogen fluoride and boron fluoride | |
US3190828A (en) | Catalytic process for cracking oils containing metallic contaminants | |
US2507861A (en) | Solvent refining of light oils | |
US1940649A (en) | Process for purifying unrefined hydrocarbon oils by action of high pressure hydrogen | |
DE2921601C2 (d) | ||
US2728712A (en) | Reforming paraffinic naphthas employing lithium, calcium, barium, or strontium | |
US2719106A (en) | Champagnat | |
US1955268A (en) | Process for preparing low boiling hydrocarbons from higher boiling hydrocarbons | |
US2752406A (en) | Removing diolefins from petroleum fractions by forming codimers with cyclic diolefins and distilling | |
US2605211A (en) | Recovering antimony trichloride from hydrocarbon extract phase | |
US2773110A (en) | Purification of paraffin hydrocarbons boiling above about 380 deg. c. |