CN2331876Y - Light-hydrocarbon liquid-state mixe gasification device - Google Patents

Light-hydrocarbon liquid-state mixe gasification device Download PDF

Info

Publication number
CN2331876Y
CN2331876Y CN 98235843 CN98235843U CN2331876Y CN 2331876 Y CN2331876 Y CN 2331876Y CN 98235843 CN98235843 CN 98235843 CN 98235843 U CN98235843 U CN 98235843U CN 2331876 Y CN2331876 Y CN 2331876Y
Authority
CN
China
Prior art keywords
gas
air
reactor
meter
ball valve
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 - Fee Related
Application number
CN 98235843
Other languages
Chinese (zh)
Inventor
赵文虎
陈尔程
赵晓波
Original Assignee
赵文虎
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 赵文虎 filed Critical 赵文虎
Priority to CN 98235843 priority Critical patent/CN2331876Y/en
Application granted granted Critical
Publication of CN2331876Y publication Critical patent/CN2331876Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

The utility model discloses a light-hydrocarbon liquid-state mixed gasification device, which is composed of an oil storage tank, a reaction kettle, a solar energy circulating water tank, an electromagnetic valve, an air filter, a fuel gas pipe, and a ball valve. The utility model is characterized in that the reaction kettle is provided with a liquefied gas pipe which is connected with a damping valve and a fuel gas meter; the fuel gas meter is connected with a liquefied gas steel cylinder via the ball valve; the reaction kettle is provided with an air tube which is connected with the air filter through an attenuator, an air flowmeter, and the electromagnetic valve; the fuel gas pipe arranged above the reaction kettle is connected with a concentration meter via the ball valve. The utility model has the advantages of simple structure, capability of using the liquefied gas as well as the mixed light hydrocarbon liquid and the liquefied gas as raw material, convenient and safe utilization, no liquid in pipelines, good gasifying effect, and high heat value of combustion gas.

Description

The liquid mixing gasifying device of lighter hydrocarbons
It is that main liquid light hydrocarbon (adding a small amount of liquefied gas) is produced air mixture with chemical by-product (carbon five) that the utility model relates to a kind of, directly flows to the liquid mixing gasifying device of lighter hydrocarbons of user's burning with pipeline with low pressure.
The gasification installation that uses has following two kinds at present: a kind of is that light-hydrocarbon gas gasification installation, this device are made of oil storage tank, reactor, combustion gas and air blending tank, air cushioning jar, electric heating water tank, air boost pump, the a small amount of crude oil of input is to reactor from oil storage tank, crude oil is through heat cycles water in the reactor, make crude oil oil temperature rise to 30~40 ℃ and gasify, air boost pump injects the air of air cushioning jar and reactor gasification burning and is transported to combustion gas and air blending tank respectively and forms and mix empty combustion gas and flow to the user by pipeline.Another kind is a Chinese patent, the patent No. is 94200723.9, Granted publication number is CN2185266Y, denomination of invention " light-hydrocarbon gas system supply equipment and pipeline ", the scheme of this patent is: the air supply pipe of light-hydrocarbon gas system supply equipment and oil return pipe communicate with fuel and vapor separator, in user mode, pressure-reducing valve is contained in roof, between fuel and vapor separator and pressure-reducing valve tracheae is housed, between pressure-reducing valve and oil return separator tracheae is housed, between oil return separator and oil storage tank oil pipe is housed, oily vapour separate measurement table and air inlet pipe and flowline communicate with tracheae, and escape pipe communicates with kitchen range.Air inlet pipe is contained between oil tank booster pump and the head tank, magnetic valve is housed on it, fuel feed pump is contained between head tank and the retort, on the water tank of retort electric heater is housed, air hose is contained between gas bag and the retort, magnetic valve is housed on it, the combustion gas booster pump is housed on the gas bag, the air supply pipe of retort communicates with light-hydrocarbon gas system supply equipment and air supply pipe, the oil return pipe of oil storage tank communicates with the oil return pipe of light-hydrocarbon gas system supply equipment, rupture pressure disc also is housed on head tank, rupture pressure disc is housed on the retort, rupture pressure disc is housed on the oil storage tank.Booster pump injects the air of air cushioning jar and sends into retort through the air isocon, in retort, form a large amount of little gas columns and fully mix the formation air mixture with the oil that injects retort, utilize hot water in the electrical heating cyclic water tank simultaneously, thereby the oil temperature in the raising retort, improve gasification result, make air mixture and be transported to the user by pipeline.Above-mentioned two kinds mainly exist following problem: 1, the fluctuation of fuel gas buring calorific value is big, because the lighter hydrocarbons liquid material is with seasonal variations, the crude oil rate of gasification increases with increase in temperature, output gas concentration fluctuating range is bigger, the fluctuation of concentration amplitude surpasses 3%, the fuel gases calorific value fluctuation surpasses 20% (promptly 500 kilocalories), and this brings certain difficulty to correct charge of resident and burning.2, the air feed number of users is restricted.General 3m 3Reactor can only be concentrated with the gas time (date for dinner in two-day weekend) for 200-250 family, particularly user, and system tolerance does not catch up with, and combustion heat value is on the low side, will supply 300-350 family or more families as a supply station, and a reactor does not satisfy.3, winter, outside air temperature was down to zero following, combustion gas is prone to liquid in the pipeline, general light-hydrocarbon gas gasification installation mixes empty than being controlled at 1: 4, the combustion gas dew point is 0~-3 ℃, but winter, outdoor temperature dropped to subzero 5 ℃ or when lower, indoor kitchen space temperature can drop to about 0 ℃, and combustion gas becomes liquid easily in the pipeline, and it will influence resident's burning or see the plug kitchen range.4, oil storage tank lacks light hydrocarbon oil and does not in time transport to, and influences the user and uses gas.
The purpose of this utility model has provided a kind of lighter hydrocarbons mixing gasifying device, the liquefaction tracheae is housed on reactor, be suitable for multiple occasion and use (scarce lighter hydrocarbons fluid oil, replace energy air feed equally with liquefied gas), increased gas gasification efficient and air feed efficient, make combustion gas and air mixing ratio less than 3%, combustion heat value control is below 10%, the combustion gas dew point drops to-7~-10 ℃, and is simple in structure, safe and reliable.
For realizing above-mentioned task, the utility model is by the following technical solutions: it is by oil storage tank, reactor, solar energy cyclic water tank, magnetic valve, air cleaner, air cushioning jar, formation such as Gas Pipe, ball valve, fuel feed pump is housed above oil storage tank, fuel feed pump connects ball valve and links to each other with reactor, reactor both sides water pipe links to each other with the solar energy cyclic water tank, and reactor one side-lower is equipped with air hose and links to each other with air cleaner through magnetic valve.It is characterized in that being equipped with the liquefaction tracheae and link to each other with attenuator, gas meter, flow meter, ball valve, cylinder for liquefied gas above reactor, the reactor top links to each other with user's kitchen range by Gas Pipe, ball valve, gas concentration degree meter.Reactor one side top air hose, attenuator, airflow meter link to each other with air cleaner.The air cushioning jar links to each other with air cleaner by air hose, and the air cushioning jar links to each other with micro-compressor by air hose.
Fig. 1 is the liquid mixing gasifying apparatus structure of a lighter hydrocarbons schematic diagram.
Below in conjunction with Fig. 1 the utility model is described in further detail.
With reference to the accompanying drawings as can be known, fuel feed pump 3 is equipped with in oil storage tank 1 top, and fuel feed pump 3 connects ball valve 2 and links to each other with reactor 17, reactor 17 both sides water pipes 22 link to each other with solar energy cyclic water tank 24, when winter, the oil temperature was lower than 15 ℃, open cyclic water tank 24, oily temperature is higher than more than 15 ℃.Reactor 17 1 sides are equipped with air hose 4,7 up and down, link to each other with air cleaner 8 through magnetic valve 5,6 and attenuator 26, airflow meter 27, air hose 7 is housed on reactor, and air hose 7 links to each other with air cleaner 8 through attenuator 26, airflow meter 27, magnetic valve 6.Air cleaner 8 links to each other with air buffer 11 by air hose 9, and air buffer 11 links to each other with micro-compressor 10 by rubber tube 25.The Gas Pipe 16 of reactor 17 tops links to each other with densimeter 14 1 ends by ball valve 15, and densimeter 14 other ends link to each other with user's kitchen range 12 by Gas Pipe 13, is defeated by user's gas concentration and is shown by densimeter 14.Liquefaction tracheae 18 is housed on reactor 17, and liquefaction tracheae 18 links to each other with decay valve 19, gas meter, flow meter 20, and gas meter, flow meter 20 links to each other with cylinder for liquefied gas 23 by ball valve 21.When gas concentration meter 14 concentration are lower than setting value, open ball valve 21, inject certain liquefied gas, make gas concentration meter 14 show that gas concentration reaches setting value.When summer oil temperature higher, gas concentration meter 14 shows that gas concentrations are higher than setting value, opens magnetic valve 6 this moment, at this moment suitably injects pure air in the reactor 17, makes that gas concentration drops to setting value in the gas concentration meter 14.When outdoor temperature is lower than subzero 5 ℃, close heat recirculated water, make oily temperature drop to being lower than 15 ℃ (gas concentration meter 14 shows that gas concentration is lower than setting value), open liquefied gas ball valve 21 and in reactor 17, inject a small amount of liquefied gas, gas concentration up to gas concentration meter 14 reaches setting value, at this moment, it is lower to be transported to the user's gas dew point, in the residential kitchen in the pipeline combustion gas can not condense into liquid.When oil storage tank lacks light hydrocarbon oil, then open ball valve 21 and magnetic valve 6 simultaneously, in reactor, inject certain proportion liquefied gas and air simultaneously, can make equally and mix empty combustion gas.
The utility model compared with prior art has following remarkable advantage: simple in structure, easy to use, peace Complete reliable. Gas combustion heat value stabilization, combustion gas and air mixing ratio precision be less than 3%, the fuel gas buring calorific value Be controlled at (namely below 250 kilocalories) below 10%, gasification result is good, the fuel gases calorific value height. Be suitable for model Enclose extensively a 3m3Reactor air feed user can diffuse into the 300-350 family. The combustion gas depoint depression to-7~-10 ℃, combustion gas no liquid in the pipeline. Light hydrocarbon oil uses up, and raw material is not in time transported to, available liquefaction Gas replaces, and continues air feed. Raw material is available liquefied gas both, and available light hydrocarbon liquid and liquefied gas mix again. This Order is safe and reliable, and gas price is low, be applicable to that the town dweller lives and the occasion such as industrial production to the gaseous fuel demand.

Claims (3)

1, the liquid mixing gasifying device of a kind of lighter hydrocarbons, it is made of oil storage tank (1), reactor (17), solar energy cyclic water tank (24), magnetic valve (5), (6), air cleaner (8), ball valve (15), it is characterized in that being equipped with on the reactor (17) liquefaction tracheae (18), liquefaction tracheae (18) links to each other with decay valve (19), gas meter, flow meter (20), and gas meter, flow meter (20) links to each other with cylinder for liquefied gas (23) by ball valve (21).
2, the liquid mixing gasifying device of a kind of lighter hydrocarbons according to claim 1, it is characterized in that being equipped with on reactor (17) air hose (7), air hose (7) links to each other with air cleaner (8) through attenuator (26), airflow meter (27), magnetic valve (6).
3, the liquid mixing gasifying device of a kind of lighter hydrocarbons according to claim 1, the Gas Pipe (16) that it is characterized in that reactor (17) top links to each other with densimeter (14) one ends by ball valve (15), and densimeter (14) other end links to each other with user's kitchen range (12) by Gas Pipe (13).
CN 98235843 1998-05-29 1998-05-29 Light-hydrocarbon liquid-state mixe gasification device Expired - Fee Related CN2331876Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 98235843 CN2331876Y (en) 1998-05-29 1998-05-29 Light-hydrocarbon liquid-state mixe gasification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 98235843 CN2331876Y (en) 1998-05-29 1998-05-29 Light-hydrocarbon liquid-state mixe gasification device

Publications (1)

Publication Number Publication Date
CN2331876Y true CN2331876Y (en) 1999-08-04

Family

ID=33984034

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 98235843 Expired - Fee Related CN2331876Y (en) 1998-05-29 1998-05-29 Light-hydrocarbon liquid-state mixe gasification device

Country Status (1)

Country Link
CN (1) CN2331876Y (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102418838A (en) * 2011-11-30 2012-04-18 华北电力大学(保定) Liquefied petroleum gas gasification system based on direct expansion type solar heat pump and application of system
CN102705703A (en) * 2012-02-03 2012-10-03 常熟市华技锅炉制造有限公司 Gas generating device
CN102847475A (en) * 2012-09-26 2013-01-02 雷汉坤 Mixed pressure tank for synthesized gas
CN109539761A (en) * 2018-11-19 2019-03-29 长春工业大学 A kind of combustion gas air feed system for drying grain
CN110566992A (en) * 2019-08-13 2019-12-13 广东富腾能源科技有限公司 Light hydrocarbon fuel gasification system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102418838A (en) * 2011-11-30 2012-04-18 华北电力大学(保定) Liquefied petroleum gas gasification system based on direct expansion type solar heat pump and application of system
CN102705703A (en) * 2012-02-03 2012-10-03 常熟市华技锅炉制造有限公司 Gas generating device
CN102847475A (en) * 2012-09-26 2013-01-02 雷汉坤 Mixed pressure tank for synthesized gas
CN109539761A (en) * 2018-11-19 2019-03-29 长春工业大学 A kind of combustion gas air feed system for drying grain
CN110566992A (en) * 2019-08-13 2019-12-13 广东富腾能源科技有限公司 Light hydrocarbon fuel gasification system

Similar Documents

Publication Publication Date Title
CN104456605B (en) Gasification device for ordinary-pressure liquid light hydrocarbons
Walsh et al. Utilization of biogas
CN2331876Y (en) Light-hydrocarbon liquid-state mixe gasification device
Bajracharya et al. Purification and compression of biogas: A research experience
CN204358766U (en) Normal pressure liquid light hydrocarbon gasification installation
CN2535679Y (en) Liquid-mmedium lifting auto-control mixed gas device made from ligt hydrocarbon oil
CN1120880C (en) Gas generating system and its usage
CN1053270C (en) Light hydrocarbon gasifying and gas-mixing system and technology
CN209622494U (en) A kind of natural gas supply regulator of asphalt mixing plant
CN1088815C (en) Pentane pipeline liquefied gas device
CN201852125U (en) Dimethyl ether gas supply device for industrial boiler
CN2229925Y (en) Low pressure transmission equipment for low molecule hydrocarbon oil
CN101265425B (en) Method for reducing heat value of gaseous liquefied natural gas
CN2636104Y (en) Light hydrocarbon gasifier
CN2145906Y (en) Civil pentane pipeline gas producer
CN208170375U (en) A kind of energy saving and environment friendly heat-producing machine and its heat-producing machine group
CN1896193A (en) Production of mixed urban gas with light-hydrocarbon gas and coal gas blending
CN103423589B (en) Liquid oxygen vaporizing system for technology of preparing methanol with coke oven gas and technology
CN1067447A (en) A kind of method and equipment thereof that pentane is converted into universal gas
CN2313160Y (en) Fuel-gas transporting device for gas-carried pentane-evaporating pipeline
KR20110042142A (en) Hybrid gas auto supply system
CN2594614Y (en) Hydrocarbon gasifier for firing ceramics
CN206310528U (en) Light hydrocarbon system for providing cleaning cloth grass steam
CN2630665Y (en) Light-oil-fuel automatic controlling device
CN2490164Y (en) Multifunction light hydrocarbon gasification cylinder

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee