RU2011123937A - METHOD FOR LIQUID DEGASATION, PREFERREDLY THERMAL WATER DEAERATION, AND DEVICE FOR ITS IMPLEMENTATION - Google Patents
METHOD FOR LIQUID DEGASATION, PREFERREDLY THERMAL WATER DEAERATION, AND DEVICE FOR ITS IMPLEMENTATION Download PDFInfo
- Publication number
- RU2011123937A RU2011123937A RU2011123937/05A RU2011123937A RU2011123937A RU 2011123937 A RU2011123937 A RU 2011123937A RU 2011123937/05 A RU2011123937/05 A RU 2011123937/05A RU 2011123937 A RU2011123937 A RU 2011123937A RU 2011123937 A RU2011123937 A RU 2011123937A
- Authority
- RU
- Russia
- Prior art keywords
- vapor
- water
- flow rate
- deaeration
- liquid
- Prior art date
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract 17
- 239000007788 liquid Substances 0.000 title claims abstract 7
- 238000000034 method Methods 0.000 title claims abstract 7
- 239000007789 gas Substances 0.000 claims abstract 8
- 238000010438 heat treatment Methods 0.000 claims abstract 6
- 239000003921 oil Substances 0.000 claims abstract 4
- 230000001105 regulatory effect Effects 0.000 claims abstract 4
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract 2
- 230000005494 condensation Effects 0.000 claims abstract 2
- 238000009833 condensation Methods 0.000 claims abstract 2
- 238000007872 degassing Methods 0.000 claims abstract 2
- 239000000295 fuel oil Substances 0.000 claims abstract 2
- 229930195733 hydrocarbon Natural products 0.000 claims abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract 2
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1. Способ дегазации жидкости, предпочтительно термической деаэрации воды, включающий деаэрацию воды при температуре насыщения, отвод газовой фазы и образовавшегося выпара, регулирование расхода которого производят пропорционально расходу исходной воды, с дальнейшей конденсацией пара и удалением несконденсированных газов, отличающийся тем, что вначале задают концентрацию остаточного газа в деаэрированной жидкости, затем рассчитывают количество выпара по расходу исходной воды и в процессе деаэрации непрерывно контролируют и поддерживают концентрацию остаточного газа за счет оптимального расхода выпара, регулируя расход греющей среды.2. Способ по п.1, отличающийся тем, что в качестве жидкости применяют нефть, мазут, продукты нефтепереработки, содержащие углеводородные пары.3. Устройство для термической деаэрации воды, включающее деаэратор с трубопроводами исходной воды и выпара, а также греющей среды и деаэрированной воды, с установленными на них датчиками расхода, регулирующий орган, отличающееся тем, что оно включает управляющий контроллер, соединенный с датчиками расхода исходной воды и выпара, а регулирующий орган установлен на трубопроводе греющей среды.1. The method of degassing a liquid, preferably thermal deaeration of water, including deaeration of water at a saturation temperature, the removal of the gas phase and the resulting vapor, the flow rate of which is proportional to the flow rate of the source water, with further condensation of the vapor and the removal of non-condensed gases, characterized in that the concentration is first set the residual gas in the deaerated liquid, then the amount of vapor is calculated from the flow rate of the source water and in the process of deaeration is continuously monitored and maintained They determine the concentration of residual gas due to the optimal flow rate of the vapor by adjusting the flow rate of the heating medium. 2. The method according to claim 1, characterized in that the liquid used is oil, fuel oil, oil products containing hydrocarbon vapors. A device for thermal deaeration of water, including a deaerator with pipelines of source water and vapor, as well as a heating medium and deaerated water, with flow sensors installed on them, a regulating body, characterized in that it includes a control controller connected to the sensors of the flow of source water and vapor , and the regulatory body is installed on the heating medium pipeline.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2011123937/05A RU2492145C2 (en) | 2011-06-10 | 2011-06-10 | Method for thermal deaeration of water and apparatus for realising said method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2011123937/05A RU2492145C2 (en) | 2011-06-10 | 2011-06-10 | Method for thermal deaeration of water and apparatus for realising said method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2011123937A true RU2011123937A (en) | 2012-12-20 |
| RU2492145C2 RU2492145C2 (en) | 2013-09-10 |
Family
ID=49165043
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2011123937/05A RU2492145C2 (en) | 2011-06-10 | 2011-06-10 | Method for thermal deaeration of water and apparatus for realising said method |
Country Status (1)
| Country | Link |
|---|---|
| RU (1) | RU2492145C2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2745212C1 (en) * | 2020-06-25 | 2021-03-22 | Наргиз Габбасович Маликов | Modular deaeration installation |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002301305A (en) * | 2001-04-03 | 2002-10-15 | Kurita Water Ind Ltd | Deaeration unit and deaerator |
| RU2233241C1 (en) * | 2003-08-05 | 2004-07-27 | Ульяновский государственный технический университет | Method of thermal deaeration of water |
| RU2241680C1 (en) * | 2003-08-05 | 2004-12-10 | Ульяновский государственный технический университет | Method of thermal deaeraton of water |
| RU2256619C1 (en) * | 2004-03-23 | 2005-07-20 | Государственное образовательное учреждение высшего профессионального образования "Ульяновский государственный технический университет" | Deaeration plant |
| RU2256620C1 (en) * | 2004-03-30 | 2005-07-20 | Государственное образовательное учреждение высшего профессионального образования "Ульяновский государственный технический университет" | Deaeration plant |
| RU2256621C1 (en) * | 2004-03-30 | 2005-07-20 | Государственное образовательное учреждение высшего профессионального образования "Ульяновский государственный технический университет" | Deaeration plant |
-
2011
- 2011-06-10 RU RU2011123937/05A patent/RU2492145C2/en active IP Right Revival
Also Published As
| Publication number | Publication date |
|---|---|
| RU2492145C2 (en) | 2013-09-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | The patent is invalid due to non-payment of fees |
Effective date: 20140611 |
|
| NF4A | Reinstatement of patent |
Effective date: 20150510 |
|
| MM4A | The patent is invalid due to non-payment of fees |
Effective date: 20160611 |
|
| NF4A | Reinstatement of patent |
Effective date: 20170523 |