GB904953A - Method and apparatus for producing continuously nitrohumic acids - Google Patents
Method and apparatus for producing continuously nitrohumic acidsInfo
- Publication number
- GB904953A GB904953A GB2637359A GB2637359A GB904953A GB 904953 A GB904953 A GB 904953A GB 2637359 A GB2637359 A GB 2637359A GB 2637359 A GB2637359 A GB 2637359A GB 904953 A GB904953 A GB 904953A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reaction
- vessel
- nitric acid
- vessels
- leads
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08H—DERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS
- C08H99/00—Subject matter not provided for in other groups of this subclass, e.g. flours, kernels
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
In the production of nitrohumic acids by continuously passing a suspension of powdered coal in dilute nitric acid (5 to 40% by weight) through a series of at least three reaction vessels, each reaction vessel is maintained under normal pressure and at a temperature from 40 DEG to 100 DEG C. and the gases (containing nitric oxide) formed in each vessel are collected in a single pipe which leads to a nitric acid recovery system wherein the nitric oxide is oxidized by air or oxygen to form nitrogen peroxide, which is then reacted with water. The first reaction vessel is heated to initiate the reaction, the next vessel is cooled because the early stages of the reaction are exothermic, and the last vessels are heated to complete the reaction. The Specification is accompanied by a drawing which shows nine reaction vessels, joined in series by overflow means, each vessel being provided with an agitator and a reflux condenser. The exhaust ends of the individual condensers are all connected to a pipe which leads to the nitric acid recovery apparatus.ALSO:In the production of nitrohumic acids by continuously passing a suspension of powdered coal in dilute nitric acid (5 to 40% by weight) through a series of at least three reaction vessels, each reaction vessel is maintained under normal pressure and at a temperature from 40 DEG to 100 DEG C. The gases (containing nitric oxide) formed in each vessel are collected in a single pipe which leads to a nitric acid recovery system. The first vessel is heated to initiate the reaction, the next vessel is cooled because the early stages of the reaction are exothermic, and the last vessels are heated in order to complete the reaction. The Specification is accompanied by a drawing which shows nine reaction vessels, joined in series by overflow means, each vessel being provided with an agitator and a reflux condenser. The exhaust ends of the individual condensers are all connected to a pipe which leads to the nitric acid recovery apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB2637359A GB904953A (en) | 1959-07-31 | 1959-07-31 | Method and apparatus for producing continuously nitrohumic acids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB2637359A GB904953A (en) | 1959-07-31 | 1959-07-31 | Method and apparatus for producing continuously nitrohumic acids |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB904953A true GB904953A (en) | 1962-09-05 |
Family
ID=10242642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB2637359A Expired GB904953A (en) | 1959-07-31 | 1959-07-31 | Method and apparatus for producing continuously nitrohumic acids |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB904953A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107722296A (en) * | 2017-11-27 | 2018-02-23 | 吴雨函 | A kind of nitro humic acid environmental protection volume production equipment |
| CN111072728A (en) * | 2019-12-30 | 2020-04-28 | 龙蟒大地农业有限公司 | Method for preparing fulvic acid by continuous nitric acid oxidation |
| CN111644127A (en) * | 2020-07-06 | 2020-09-11 | 河南黑色生态科技有限公司 | Production system and production process for preparing nitrohumic acid through oxidative degradation |
| CN115072744A (en) * | 2022-08-08 | 2022-09-20 | 山西小禹植物营养科技有限公司 | Production process for by-products of sodium nitrate and sodium nitrite in production process of nitro humic acid |
-
1959
- 1959-07-31 GB GB2637359A patent/GB904953A/en not_active Expired
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107722296A (en) * | 2017-11-27 | 2018-02-23 | 吴雨函 | A kind of nitro humic acid environmental protection volume production equipment |
| CN111072728A (en) * | 2019-12-30 | 2020-04-28 | 龙蟒大地农业有限公司 | Method for preparing fulvic acid by continuous nitric acid oxidation |
| CN111644127A (en) * | 2020-07-06 | 2020-09-11 | 河南黑色生态科技有限公司 | Production system and production process for preparing nitrohumic acid through oxidative degradation |
| CN115072744A (en) * | 2022-08-08 | 2022-09-20 | 山西小禹植物营养科技有限公司 | Production process for by-products of sodium nitrate and sodium nitrite in production process of nitro humic acid |
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