SU452726A1 - The method of obtaining cold - Google Patents
The method of obtaining coldInfo
- Publication number
- SU452726A1 SU452726A1 SU1888159A SU1888159A SU452726A1 SU 452726 A1 SU452726 A1 SU 452726A1 SU 1888159 A SU1888159 A SU 1888159A SU 1888159 A SU1888159 A SU 1888159A SU 452726 A1 SU452726 A1 SU 452726A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- condensate
- component
- obtaining cold
- low
- boiling
- Prior art date
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Separation By Low-Temperature Treatments (AREA)
Description
Изобретение относитс к холодильной технике. Известны способы получени холода путем насыщени под давлением высококип щего компонента низкокип шим и отвода выдел ющегос при насыщении тепла с последующим снижением давлени полученной смеси и испарением из последней низкоки п щего компонента. Предлагаемый способ отличаетс от из- вестных тем, что в качестве высококип ще- го компонента используют углеводородный конденсат, а в качестве низко кип щего - природный газ, и насыщение ведут под давлением от 3 до ЗОО атмосфер до коццентра ции соответственно от 30 до 240 м газа на 1м конденсата. Такой способ позвол ет повысить экономичность охлаждени природного газа в мео те его добычи. Углеводородный абсорбент (конденсат) насыщают под давлением от 3 до ЗОО атм легкими компонентакш. Насыщенный газом конденсат охлаждают и направл ют через дроссель, в котором снижаетс его давление , в теплообменник-испаритель. Полученный в последнем холод отвод т на охлаждение природного газа или непосредственно, или с помощью промежуточного теплоносител ; Предмет изобретени Способ получени холода путем насыщени под давлением высококип1пцего компонента низкокип щим и отвода выдел ющегос при насыщении тепла с последующим снижением давлени получе шой смеси и испарением из последней низкокип щего компонента , отличающийс тем, что, с целью повышени экономичности охлаждени природного газа в месте его добычи, в качест ве высококип щего компонента используют углеводородный конденсат, а в качестве низкокип ццего - природный газ, и насыщение ведут под давлением от 3 до ЗОО атм до концентрации соответственно от 30 до 240 м газа на 1 м конденсата.The invention relates to refrigeration. Methods are known for producing cold by saturating a high-boiling component with low boiling under pressure and removing heat released during saturation, followed by reducing the pressure of the resulting mixture and evaporating from the latter a low-melting component. The proposed method differs from the known ones in that hydrocarbon condensate is used as a high-boiling component, and natural gas is used as a low-boiling component, and saturation is carried out under pressure from 3 to 30% atmospheres to concentration, respectively, from 30 to 240 m. gas per 1m condensate. Such a method makes it possible to increase the economics of cooling natural gas during its production. Hydrocarbon absorbent (condensate) is saturated under pressure from 3 to 30% atm with light components. The gas-saturated condensate is cooled and sent through a choke, in which its pressure is reduced, to a heat exchanger-evaporator. The cold obtained in the latter is withdrawn to cool the natural gas either directly or by means of an intermediate heat transfer medium; The subject of the invention. A method for producing cold by saturating a high boiling point component with a low boiling point and removing heat released during saturation, followed by decreasing the pressure of the resulting mixture and evaporating it from the last low boiling point component. hydrocarbon condensate is used as a high-boiling component, and natural gas is used as a low-boiling point, and saturation is carried out under pressure from 3 to 25 a.m. The values are respectively from 30 to 240 m of gas per 1 m of condensate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1888159A SU452726A1 (en) | 1973-01-05 | 1973-01-05 | The method of obtaining cold |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1888159A SU452726A1 (en) | 1973-01-05 | 1973-01-05 | The method of obtaining cold |
Publications (1)
Publication Number | Publication Date |
---|---|
SU452726A1 true SU452726A1 (en) | 1974-12-05 |
Family
ID=20543927
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1888159A SU452726A1 (en) | 1973-01-05 | 1973-01-05 | The method of obtaining cold |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU452726A1 (en) |
-
1973
- 1973-01-05 SU SU1888159A patent/SU452726A1/en active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2250925A (en) | Process for the separation of acetylene from admixture with ethylene | |
US1469447A (en) | Absolute alcohol | |
GB636279A (en) | A process for absorbing volatile hydrocarbons from mixed gases | |
GB1421361A (en) | Vapour stripping and recovery method and apparatus | |
US2545778A (en) | Process for the preparation of krypton-rich gases | |
ES348699A1 (en) | Process for recovering acrolein by quenching,absorption and plural distillation | |
GB958191A (en) | A method of processing a mixture of liquefied gases | |
US3266219A (en) | Removal of acid constituents from gas mixtures | |
SU452726A1 (en) | The method of obtaining cold | |
GB401531A (en) | Separation of acetylene | |
JPS54115691A (en) | Liquefied carbon dioxide producing equipment | |
GB747411A (en) | Improvements relating to the separation of gases | |
GB978578A (en) | Low temperature refrigeration in ethylene plants | |
ES317591A1 (en) | Procedure for refrigerating a substance in an apparatus provided with compressor, condenser and evaporator. (Machine-translation by Google Translate, not legally binding) | |
SU61053A1 (en) | The method of obtaining oxygen | |
KR840004536A (en) | Method for preparing acid stable zeolite and high silica zeolite produced thereby | |
FR2137412A1 (en) | Separation of nitrogen from natural gas - by low temp rectification, with methane stream produced at required delivery pres | |
SU785292A1 (en) | Method of preparing 1-methoxy-1-buten-3-yn | |
SU116515A1 (en) | Urea production method | |
SU386838A1 (en) | METHOD FOR PRODUCING CARBON DIOXIDE | |
SU485289A1 (en) | The method of obtaining low-temperature cold | |
SU1120149A1 (en) | Method of obtaining oxygen | |
JPS54102287A (en) | Distilling method | |
JPS5225806A (en) | Method and appapatus for the desalting of crude oil | |
SU109714A1 (en) | Method of cleaning excess ammonia distilled from the water production of urea from carbon dioxide and water |