CN104990293A - Gas soluble water separation technology device - Google Patents
Gas soluble water separation technology device Download PDFInfo
- Publication number
- CN104990293A CN104990293A CN201510389796.9A CN201510389796A CN104990293A CN 104990293 A CN104990293 A CN 104990293A CN 201510389796 A CN201510389796 A CN 201510389796A CN 104990293 A CN104990293 A CN 104990293A
- Authority
- CN
- China
- Prior art keywords
- water
- dissolved air
- knockout drum
- air water
- natural gas
- 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.)
- Pending
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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E10/00—Energy generation through renewable energy sources
- Y02E10/10—Geothermal energy
Landscapes
- Physical Water Treatments (AREA)
Abstract
The invention provides a gas soluble water separation technology device which comprises an integrated separation tank, a natural gas burner, a heat exchange component, a water level gauge or a thermometer and multiple valves. The integrated separation tank is provided with a gas soluble water inlet, a water outlet and a natural gas outlet. The heat exchange component is further arranged in the separation tank. Natural gas enters the natural gas burner to be burned, generated heat is used for heating the heat exchange component so as to heat water in the separation tank, and finally hot water flows out of the water outlet, so that separation and full utilization of the natural gas are achieved. According to the gas soluble water separation technology device, separated gas does not need to be stored or transported, safety is improved, and investment is reduced. The temperature of geothermal water is increased through burned natural gas, and the geothermic heat value is increased.
Description
Technical field
The present invention relates to the process facility of geothermal water recovery, disposal and utilization.
Background technology
The use of underground heat more and more obtains the attention of people, and underground heat obtains the energy mainly through recovery of subterranean hot water or steam, and part underground heat also exists Water Soluble Gas, and this part GEOTHERMAL WATER is referred to as dissolved air water, namely contains the gases such as natural gas from the hot water water of underground.To in this kind of dissolved air water geothermal exploitation process, because in dissolved air water, natural gas content is relatively low, natural gas is separated and is used and just there is no good economic benefit, natural gas belongs to flammable explosive gas simultaneously, therefore need in hot water use procedure this part gas separaion out, to reduce potential safety hazard; And the gas reclaimed is transporting or in use all will consider security requirement, this all can increase extra investment.Therefore, how being separated the natural gas in Water Soluble Gas better and isolated natural gas is made full use of, is need those skilled in the art to go the problem solved to produce good economic benefit, environmental benefit and safety benefit.
Application number: the utility model of 2014206675398 belongs to technical field of environment protection equipment, be specifically related to a kind of dissolved air water release, comprise release housing, upper cover is connected with above described release housing, this upper cover upper end is tubing string, lower end and release housing match, and are connected with the first disk, the second disk, lower cover in described release housing from top to bottom in turn; Described release casing peripheral is provided with the first annulus, and described first disc centre has aperture, and described second disk is circumferentially evenly provided with circular hole, under be covered with the second annulus about center of circle symmetry.
Application number: the utility model of 2011204550229 discloses a kind of for the degassing tank in water-soluble gas geothermal water degassing device, solves the problem of water-soluble gas type geothermal water degasification technique without special equipment; The bottom of the tank interior water inlet pipe mouth of this degassing tank arranges grid, the bottom of grid arranges at least one feed distribution dish, described feed distribution dish is butterfly, comprise at the bottom of butterfly and butterfly limit, butterfly limit is uniformly distributed along the circumference some circular holes, these circular hole place planes, lower than place, butterfly limit plane, arrange baffle plate in addition around the outlet of tank interior de aerated water.
The invention of application number: 201310311672X relates to the system and method for a kind of carbon dioxide injection exploitation Water Soluble Gas.The system of carbon dioxide injection exploitation Water Soluble Gas comprises: producing well, Injection Well, moisture trap, methane/carbon dioxide gas separator, carbon dioxide/water mixer, supercharging injection pump, produced fluid pipeline; The carbon dioxide trapped and injection water are carried out high pressure mixing or only carbon dioxide are formed supercritical carbon dioxide under High Pressure by carbon dioxide/water mixer; Carbon dioxide/water mixer is connected with supercharging injection pump by pipeline; The injection fluid formed in carbon dioxide/water mixer injects Water Soluble Gas reservoir by Injection Well pit shaft after the further supercharging of supercharging injection pump, and the fluid in the water-soluble gas reservoir of displacement realizes carbon dioxide geological simultaneously and buries.
The speed that the equipment of above-mentioned several patent is separated with aqueous vapor in method is lower, is separated and recycles synchronously to complete, and this is divided gas flow and liquid only, and underuse the gas of release, the level of resources utilization is lower.
Summary of the invention
Goal of the invention:
Overcome water, gas in traditional geothermal water gathering-device can not effectively be separated, can not use by safe ready after being separated, the shortcomings such as isolated natural gas accumulating difficulty, a kind of process unit that fully can be separated natural gas in dissolved air water is provided, and handle is from the isolated natural gas combustion (of oil) insitu of Water Soluble Gas separator, improve the temperature of dissolved air water in device, realize the utilization completely of natural gas and hot water in Water Soluble Gas.
Technical scheme:
Dissolved air water Separation process arrangements disclosed by the invention, dissolved air water (or claiming Water Soluble Gas) from geothermal well first can be inputted this device, realize being separated of water and natural gas, and handle is from the isolated natural gas combustion (of oil) insitu of Water Soluble Gas separator, for the dissolved air water in heating and separating device, improve the temperature of dissolved air water in device, realize natural gas in Water Soluble Gas and be almost separated completely with hot water.This device has integrated knockout drum, neat gas burner, heat exchanger components or has water-level gauge (or thermometer) and many valves.
Integration knockout drum leaves dissolved air water access port and delivery port, and gas outlet (discharging to facilitate the natural gas separated in dissolved air water), the dissolved air water of internal reservoir through being separated of knockout drum, knockout drum inside also has heat exchanger components, gas outlet natural gas out (relies on the pressure in integrated knockout drum to be carried by natural gas line, also can supporting natural gas boosting blower fan, the discharge being beneficial to natural gas be separated, pressure in the integrated knockout drum of further reduction) enter neat gas burner burning, its heat produced is used for heating this heat exchanger components, and then add the water of hot knock-out pot inside, finally flowed out from delivery port by the hot water after heating, realize the separation of natural gas and make full use of.Hot water by hot water effluent's transport pump to heating equipment or user.
The dissolved air water of the lower storage of knockout drum is owing to being heated, and temperature improves, and is more conducive to natural gas and evaporates further from water and separate, natural gas content is wherein lowered further.In addition, natural gas line can be installed purifying device for natural gas (such as: dewater steam device), also internally piloted valve and natural gas flowmeter can be installed.
Integral separation device inside can be connected with water-level gauge and measure water level, is externally connected to control device and controls, ensure that separator there will not be dry combustion method phenomenon.
Preferably adopt pressure release separate mode in knockout drum, the pressure of the dissolved air water of namely coming from pipeline is higher than the pressure in knockout drum;
Accelerate for making the gas in dissolved air water to be separated with make to be separated more thorough, can take to install measures such as filling filler in knockout drum, filler can select the fillers such as Boolean ring, open column shape object or turbulence plate, filler has larger porosity and larger specific area, such as: porosity is greater than 80%.Filler requires to possess corrosion resistance, possesses certain structural strength and on-deformable feature in hot water.
Dissolved air water can absorb the heat in water in the process of release natural gas due to gasification, the temperature of dissolved air water will slightly reduce; Utilize combustion of natural gas to heat dissolved air water again, ensure to be separated rear dissolved air water temperature higher than inflow temperature, natural gas will be conducive to and discharge from dissolved air water and be separated.Time such as: when gas-water ratio 1:1(volume ratio), consider the latent heat heat absorption in thermal losses factor and natural gas separation process, water temperature can be made to raise about 2 ~ 6 DEG C.
The shell of dissolved air water knockout drum can be provided with heat-insulation system, and each pipeline also can have insulation, prevents the loss of heat.
Emptying interface can be installed in the bottom of knockout drum, to get rid of inner ponding, also can get rid of the solid residues such as the part silt that dissolved air water brings.
The delivery port of dissolved air water separator supporting can install out water pump, is controlled the water level of dissolved air water separator inside by the flow controlling water pump, and adapts to the change of amount of inlet water.
Many valves are preferably internally piloted valve, the preferred VFC of Flow-rate adjustment going out water pump regulates, internally piloted valve with go out water pump and be connected respectively and be controlled by self-con-tained unit, self-con-tained unit separately has many holding wires to be connected to temperature sensor (or thermometer) on knockout drum and level sensor (or water-level gauge), experiences and transmits the liquid level data in water temperature and knockout drum.By control and the adjustment of automatic control dress system, the water level in the water flow of aqueous vapor separating rate, separation degree, hot water, knockout drum is made to obtain Effective Regulation.
Whole device can pass through automatic dispatching, makes the pump head of geothermal well, flow, and the lift of hot water variable frequency pump, flow, and the temperature of dissolved air water is operated in optimum condition and optimal balance point, realizes heating efficiency and maximizes.Heated by natural gas is continuous or interval work mode, ensures that isolated Water Soluble Gas can be burnt in time, does not have Water Soluble Gas emptying, and can realize unmanned and digitlization geothermal heating.
Integration knockout drum, neat gas burner, heat exchanger components etc. can be arranged on an integral skid block, convenient mobile and with the in-site installation of geothermal well, reduce in-site installation and connect workload, reduce installation process to the impact of nearby residents.
Beneficial effect:
The present invention is exactly the natural gas by isolating in Water Soluble Gas, and natural gas is used for heating the hot water from underground heat at once, does not need to carry out natural gas storing and transport to isolated, adds security, decrease investment.The natural gas of burning improves geothermal water temperature, adds calorie value and the grade of underground heat, decreases amount of groundwater mining, reduces and promotes dissolved air water and recharge dissolved air water power consumption, add economic performance.And be separated later underground water natural gas content and greatly reduce, decrease the natural gas leaking of underground heat in use procedure, add the safety in utilization to dissolved air water underground heat.The impact of natural gas volatilization on environment that isolated natural gas passes through to have burnt less, adds environmental benefit.
The present invention solves the comprehensive utilization of dissolved air water, realizes geothermal energy resources and maximizes, improve economic benefit.
Natural gas is separated in system immediately with water, immediately burns, and reduces potential safety hazard and the safety measure investment of natural gas storing.In dissolved air water, the separation of natural gas is greater than 80%, even reaches the separate targets of more than 95%.Heating fuel, without the need to outer confession, is saved use cost and makes full use of natural resources.
Accompanying drawing explanation
Fig. 1 is in planar structure schematic diagram (pending) figure of the present invention, 1-geothermal well; 2-valve; 3-desilting separator; The emptying interface of 4-; 5-gas outlet; 6-dissolved air water access port 7-filler; 8-integration knockout drum; 9--water-level gauge (or thermometer) thermometer; 10-neat gas burner; 11-vavuum pump or booster fan; 12-heat exchanger components; 13-delivery port; 16-goes out water pump; 17-heating equipment.
Detailed description of the invention
Dissolved air water Separation process arrangements as shown in Figure 1, has integrated knockout drum 8, neat gas burner 10, heat exchanger components 12, many valves 2; Integration knockout drum 8 leaves dissolved air water access port 6, delivery port 13, gas outlet 5, the dissolved air water of internal reservoir through being separated of knockout drum 8, knockout drum 8 inside has heat exchanger components 12, gas outlet 5 natural gas out enters neat gas burner 10 and burns, its heat produced is used for heating this heat exchanger components 12, and then add the water of hot knock-out pot inside, finally flowed out from delivery port 13 by the water after heating, realize the separation of natural gas and make full use of.
Integration knockout drum 8 is internally connected with water-level gauge 9, is externally connected to control device.The delivery port 13 of dissolved air water separator is supporting installs out water pump 16, is controlled the water level of dissolved air water separator inside by the flow controlling water pump 16.The filler 7 of open column shape object is installed in knockout drum 8, has and be greater than the porosity of 80% and larger specific area.This dissolved air water separator by from after the dissolved air water input of geothermal well, can realize fully being separated, without the need to reclaiming and transport the natural gas separated separately of water and natural gas.
Claims (8)
1. a dissolved air water Separation process arrangements, can input this device by the dissolved air water from geothermal well, realize being separated of water and natural gas, it is characterized in that: this device has integrated knockout drum, neat gas burner, heat exchanger components, many valves; Integration knockout drum leaves dissolved air water access port, delivery port, gas outlet, the dissolved air water of internal reservoir through being separated of knockout drum, knockout drum inside also has heat exchanger components, gas outlet natural gas out enters neat gas burner burning, its heat produced is used for heating this heat exchanger components, and then add the water of hot knock-out pot inside, finally flowed out from delivery port by the hot water after heating, realize the separation of natural gas and make full use of.
2. dissolved air water Separation process arrangements as claimed in claim 1, is characterized in that: integral separation device is internally connected with water-level gauge, is externally connected to control device, ensure that separator there will not be dry combustion method phenomenon.
3. dissolved air water Separation process arrangements as claimed in claim 1, is characterized in that: adopt pressure release separate mode in knockout drum, and the pressure of the dissolved air water of namely coming from pipeline is higher than the pressure in knockout drum.
4. dissolved air water Separation process arrangements as claimed in claim 1, is characterized in that: in knockout drum, be provided with filling filler, and filler has and is greater than the porosity of 80% and larger specific area.
5. dissolved air water Separation process arrangements as claimed in claim 4, is characterized in that: filler is Boolean ring, open column shape object or turbulence plate.
6. dissolved air water Separation process arrangements as claimed in claim 1, is characterized in that: the delivery port of dissolved air water separator is supporting installs out water pump, is controlled the water level of dissolved air water separator inside by the flow controlling water pump.
7. the dissolved air water Separation process arrangements as described in claim 1 and 6, it is characterized in that: many valves are internally piloted valve, the Flow-rate adjustment going out water pump is that VFC regulates, internally piloted valve with go out water pump and be connected respectively and be controlled by self-con-tained unit, self-con-tained unit separately has holding wire to be connected to temperature sensor on knockout drum or water-level gauge, experience and transmit the liquid level data in water temperature or knockout drum, by the control of automatic control dress system with regulate water level in the water flow of aqueous vapor separating rate, separation degree, hot water or knockout drum.
8. the dissolved air water Separation process arrangements as described in claim 1,2,3 and 6, is characterized in that: described integrated knockout drum, neat gas burner, heat exchanger components are arranged on an integral skid block, convenience movement and the in-site installation with geothermal well.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510389796.9A CN104990293A (en) | 2015-07-06 | 2015-07-06 | Gas soluble water separation technology device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510389796.9A CN104990293A (en) | 2015-07-06 | 2015-07-06 | Gas soluble water separation technology device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN104990293A true CN104990293A (en) | 2015-10-21 |
Family
ID=54302144
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510389796.9A Pending CN104990293A (en) | 2015-07-06 | 2015-07-06 | Gas soluble water separation technology device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104990293A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107807204A (en) * | 2017-09-28 | 2018-03-16 | 中国石油天然气集团公司 | The CH_4 detection real-time sampling device suitable for the cbm development process mining mouth of a river |
CN108689443A (en) * | 2018-07-05 | 2018-10-23 | 中铁二院昆明勘察设计研究院有限责任公司 | A kind of separator of underground water and pernicious gas |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1366128A (en) * | 2002-03-08 | 2002-08-28 | 大庆方兴投资有限责任公司 | Gas-water separation method for geothermal water |
CN202322421U (en) * | 2011-11-16 | 2012-07-11 | 东北石油大学 | Degassing tank for water-soluble gas geothermal water degassing device |
CN202315428U (en) * | 2011-11-16 | 2012-07-11 | 东北石油大学 | Water-soluble gas type geothermal water degasser |
CN103343678A (en) * | 2013-07-23 | 2013-10-09 | 中国石油大学(华东) | System and method for exploiting water-soluble gas by injecting carbon dioxide |
CN203694676U (en) * | 2013-12-26 | 2014-07-09 | 金大地新能源(天津)集团有限公司 | Geothermal water degassing device of geothermal water heat supply system |
CN204251375U (en) * | 2014-11-11 | 2015-04-08 | 中国石油天然气股份有限公司 | Dissolved air water releaser |
CN204902294U (en) * | 2015-07-06 | 2015-12-23 | 上海亿景能源科技有限公司 | Dissolve gas -water separation device |
-
2015
- 2015-07-06 CN CN201510389796.9A patent/CN104990293A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1366128A (en) * | 2002-03-08 | 2002-08-28 | 大庆方兴投资有限责任公司 | Gas-water separation method for geothermal water |
CN202322421U (en) * | 2011-11-16 | 2012-07-11 | 东北石油大学 | Degassing tank for water-soluble gas geothermal water degassing device |
CN202315428U (en) * | 2011-11-16 | 2012-07-11 | 东北石油大学 | Water-soluble gas type geothermal water degasser |
CN103343678A (en) * | 2013-07-23 | 2013-10-09 | 中国石油大学(华东) | System and method for exploiting water-soluble gas by injecting carbon dioxide |
CN203694676U (en) * | 2013-12-26 | 2014-07-09 | 金大地新能源(天津)集团有限公司 | Geothermal water degassing device of geothermal water heat supply system |
CN204251375U (en) * | 2014-11-11 | 2015-04-08 | 中国石油天然气股份有限公司 | Dissolved air water releaser |
CN204902294U (en) * | 2015-07-06 | 2015-12-23 | 上海亿景能源科技有限公司 | Dissolve gas -water separation device |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107807204A (en) * | 2017-09-28 | 2018-03-16 | 中国石油天然气集团公司 | The CH_4 detection real-time sampling device suitable for the cbm development process mining mouth of a river |
CN107807204B (en) * | 2017-09-28 | 2020-02-14 | 中国石油天然气集团公司 | Real-time sampling device suitable for methane detection in drainage and production water gap in coal bed gas development process |
CN108689443A (en) * | 2018-07-05 | 2018-10-23 | 中铁二院昆明勘察设计研究院有限责任公司 | A kind of separator of underground water and pernicious gas |
CN108689443B (en) * | 2018-07-05 | 2023-07-25 | 中铁二院昆明勘察设计研究院有限责任公司 | Separation device for underground water and harmful gas |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN204902294U (en) | Dissolve gas -water separation device | |
CN203731530U (en) | Recycling system of boiler discharge water thermal energy and steam condensation water | |
CN104990293A (en) | Gas soluble water separation technology device | |
CN202188476U (en) | Electrode boiler | |
CN109654581A (en) | A kind of Combined heating system of the cross-season heat-storage based on artesian aquifer | |
CN111911117B (en) | Combustible ice exploitation pipe column heated by stratum energy and operation method thereof | |
CN108590612A (en) | A kind of super burn heater for oil shale in-situ cracking | |
CN208330328U (en) | A kind of system for oil shale in-situ cracking | |
CN205279228U (en) | Utilize solar water heater to store hot water heating room | |
CN204345944U (en) | A kind of water storage box type self-loopa solar water heater | |
CN205245140U (en) | Weary gas recovery unit and recovery system | |
CN204901730U (en) | Device is recycled to workshop hot water heat energy | |
CN201535543U (en) | Microcomputer electric heating water heater | |
CN114001465A (en) | Solar crude oil heating composite system and method for adjusting soil temperature field balance | |
CN207741335U (en) | A kind of exhaust gases combustion heating waste oil device | |
CN208546278U (en) | A kind of novel dry-hot-rock geothermal quarrying apparatus | |
CN203249382U (en) | Automatic circulating energy-saving hot water furnace | |
CN208619096U (en) | A kind of super burn heater for oil shale in-situ cracking | |
CN207365170U (en) | Rural Families coal and electricity dual-purpose energy-saving micro safety normal-pressure hot water heating boiler | |
CN209507651U (en) | A kind of water-soluble air separation of mid-deep strata GEOTHERMAL WATER | |
CN105258193A (en) | Water heating device using waste heat of range hood | |
CN206190273U (en) | Shaft bottom water -discharging and gas -producing unit | |
CN206207397U (en) | A kind of Industrial Boiler oxygen-eliminating device optimizes system | |
CN205424882U (en) | Double -furnace courage steam generator | |
CN207330968U (en) | Hot steel slag cracking stove pressurized, heated bell |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151021 |