CN2246235Y - Cold micro-pressuring pipeline transport appts. for forming gas - Google Patents

Cold micro-pressuring pipeline transport appts. for forming gas Download PDF

Info

Publication number
CN2246235Y
CN2246235Y CN 96229197 CN96229197U CN2246235Y CN 2246235 Y CN2246235 Y CN 2246235Y CN 96229197 CN96229197 CN 96229197 CN 96229197 U CN96229197 U CN 96229197U CN 2246235 Y CN2246235 Y CN 2246235Y
Authority
CN
China
Prior art keywords
tank
gas
pipeline
oil
communicated
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 96229197
Other languages
Chinese (zh)
Inventor
过柏华
焦天香
顾中兴
徐济鋆
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN 96229197 priority Critical patent/CN2246235Y/en
Application granted granted Critical
Publication of CN2246235Y publication Critical patent/CN2246235Y/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 relates to a cold micro-pressuring pipeline transport apparatus for forming gas which converts the light hydrocarbon oil into fuel gas, composed of a light hydrocarbon oil storage tank, a gasification tank, an automatic control mechanism, a low-voltage pressure pump, and a gas storage tank which are connected through pipelines. The lower end of the oil storage tank is communicated with the gasification tank through the valve pipeline, and the gasification tank is communicated with the gas storage tank through pipelines. The low-voltage pressure pump controlled by the automatic control mechanism is communicated with the gasification tank through the valve pipeline. The automatic control mechanism controls the manometer through the fuel gas, communicating with the gas storage tank through pipelines, and the gas storage tank is provided with an outlet. The utility model has the characteristics of low investment cost, few land occupation, etc.

Description

The little capstan feedway of synthetic gas normal temperature
The utility model relates to a kind of Petro-Chemical Machinery device, is a kind of little capstan feedway of synthetic gas normal temperature that light hydrocarbon oil is changed into combustion gas specifically.
The conveyance conduit network equipment that produces town gas and coal gas is a kind of huge engineering that needs country or local government's substantial contribution to drop into, and need occupy the soil or the farmland in city or suburb.Bottled gas need dispose canned station, the canned device of high pressure and dispensing apparatus; and owing to tanked liquefied fuel need be stored under high pressure (1.5MP) cryogenic conditions; thereby must satisfy safety requirement such as explosion-proof, anti-flaming; therefore the reconnaissance of building a station needs certain insulation blocking district; often build suburbs in, need bigger space, place, though cost is more much smaller than the city; but need government department to support investment equally, depending merely on user's fund-raising is difficult the realization.
The purpose of this utility model is to provide a kind of and changes into industrial light hydrocarbon oil and the little capstan feedway of synthetic gas normal temperature domestic gas, and it is low that this device has cost of investment, takes up an area of characteristics such as few.
To achieve these goals, the utility model adopts following technological scheme: the little capstan feedway of a kind of synthetic gas normal temperature, it is characterized in that: it is by the light hydrocarbon oil oil tank, gasifying tank, automatic control mechanism, low pressure compression pump and gas tank connect to form through pipeline, the light hydrocarbon oil oil tank is provided with oil-feed stop valve and oil tank pressure gauge, its lower end is communicated with gasifying tank through pipeline, be provided with the oil-feed stop valve that gentleization of oil cut-off valve jar of oil tank in this pipeline, gasifying tank is provided with the gasifying tank pressure gauge, gasifying tank is communicated with gas tank through pipeline, low pressure compression pump through the automatic control mechanism controls is communicated with gasifying tank by pipeline, be provided with Electric Actuated Stop Valves in this pipeline successively, the little pressure cutoff valve that adds of safety check and air inlet, automatic control mechanism is communicated with gas tank through combustion gas pilot pressure table and pipeline, and gas tank is provided with delivery outlet.
Good effect of the present utility model is: adopt special process, with light hydrocarbon oil under the little pressurized conditions of normal temperature, gasify the back with non-combustible gas synthesize civilian or industrial inflammable gas, so capital investment reduces greatly, there is not high-pressure installation again, do not need government investment, only build, estimate 2,000 yuan of the expense of opening an account each households by present price by user's fund-raising mode; Device occupied ground space is few, in the customer volume at 5000 families, and occupied ground 250-300m 2Because the fuel that uses is nontoxic, the gasification and the conveying of this device of process are the low pressure non-toxic gas, and not entail dangers to people's life is leaked in user's improper use, and operating conditions low pressure so can not blast, can not cause a serious accident; Compare with bottled gas, also do not need to economize the labour force because of ventilation carrying steel cylinder; Because fuel price calorific value low and fuel is higher, the same terms can be saved 10% expenditure down.
Below in conjunction with drawings and Examples the utility model is elaborated.
Accompanying drawing is the structural representation of a preferred embodiment of the utility model.
See also shown in the accompanying drawing, the utility model is by light hydrocarbon oil oil tank 10, gasifying tank 20, automatic control mechanism 30, low pressure compression pump 40 and gas tank 50 connect to form through pipeline, the light hydrocarbon oil oil tank is provided with oil-feed stop valve 11 and oil tank pressure gauge 12, its lower end is communicated with gasifying tank through pipeline 1, be provided with the oil-feed stop valve 21 that oil cut-off valve 13 and gasifying tank of oil tank in this pipeline, gasifying tank is provided with gasifying tank pressure gauge 22, gasifying tank is communicated with gas tank through pipeline 2, low pressure compression pump through the automatic control mechanism controls is communicated with gasifying tank by pipeline 3, be provided with Electric Actuated Stop Valves 41 in this pipeline successively, the little pressure cutoff valve 43 that adds of safety check 42 and air inlet, automatic control mechanism is communicated with gas tank through combustion gas pilot pressure table 31 and pipeline 4, and gas tank is provided with delivery outlet 51.
When the utility model uses, with (the oil tank of packing into of its vapour tension≤0.1MP) of the light hydrocarbon oil after the allotment, enter gasifying tank through valve pipe, keep certain liquid level height in jar, gasifying tank utilization special process technology gasifies light hydrocarbon oil under the little pressurized conditions of normal temperature, (non-combustible gas of the device output of 0.05MP~0.2MP) mixes with the light hydrocarbon oil steam in the gasifying tank through the low pressure compression pump of automatic control mechanism controls, become inflammable gas, deliver to gas tank through being connected of valve and pipeline, by gas tank combustible gas is entered the gas transmission pipeline network network behind reduction valve, deliver to user terminal.Gasifying tank is liquid fuel gasification in the utility model system, feeds the gas of non-combustible in static jar, and the steam output of accelerating liquid can foundation: P 2-P 1The formula of=2 σ/r, and the pressure P of the gasifying tank liquid level gross area and little pressurization 1, flow, the surface tension coefficient σ of this fuel liquid phase and the bubble radius r of little superheated steam obtain total gas quantity, P in the formula 2Be little pressurization back fuel bubble inner pressure power.Low pressure compression pump and automatic control mechanism form little pressurization generating means, automatic control mechanism guarantees that the utility model can enter automatic tracking management, can enter auto state after administrative staff start this device, by the working pressure output combustion gas of setting, gaseous-pressure is 0.02MP+0.005~-0.01.When operation was in automatic Control work state, the demonstration of gasifying tank liquid level, hi-lo signal alarm, malfunction alarm, function such as pressurization automatically all had automatic control mechanism two-way to control, and guarantee the normal air feed of device.The effect of gas tank is a combustible gas of storing the gasifying tank output, and keeps the stable of supply gas pressure, plays the effect of air storage and voltage stabilizing.

Claims (1)

  1. The little capstan feedway of a kind of synthetic gas normal temperature, it is characterized in that: it is by light hydrocarbon oil oil tank (10), gasifying tank (20), automatic control mechanism (30), low pressure compression pump (40) and gas tank (50) connect to form through pipeline, the light hydrocarbon oil oil tank is provided with oil-feed stop valve (11) and oil tank pressure gauge (12), its lower end is communicated with gasifying tank through pipeline (1), be provided with the oil-feed stop valve (21) that oil cut-off valve (13) and gasifying tank of oil tank in this pipeline, gasifying tank is provided with gasifying tank pressure gauge (22), gasifying tank is communicated with gas tank through pipeline (2), low pressure compression pump through the automatic control mechanism controls is communicated with gasifying tank by pipeline (3), be provided with Electric Actuated Stop Valves (41) in this pipeline successively, the little pressure cutoff valve (43) that adds of safety check (42) and air inlet, automatic control mechanism is communicated with gas tank through combustion gas pilot pressure table (31) and pipeline (4), and gas tank is provided with delivery outlet (51).
CN 96229197 1996-01-30 1996-01-30 Cold micro-pressuring pipeline transport appts. for forming gas Expired - Fee Related CN2246235Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 96229197 CN2246235Y (en) 1996-01-30 1996-01-30 Cold micro-pressuring pipeline transport appts. for forming gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 96229197 CN2246235Y (en) 1996-01-30 1996-01-30 Cold micro-pressuring pipeline transport appts. for forming gas

Publications (1)

Publication Number Publication Date
CN2246235Y true CN2246235Y (en) 1997-01-29

Family

ID=33906902

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 96229197 Expired - Fee Related CN2246235Y (en) 1996-01-30 1996-01-30 Cold micro-pressuring pipeline transport appts. for forming gas

Country Status (1)

Country Link
CN (1) CN2246235Y (en)

Similar Documents

Publication Publication Date Title
CN101479150B (en) Fuel system for gas driven vessel
US5924283A (en) Energy management and supply system and method
CN101520128B (en) Movable type method and device for supplying liquid phase natural gas and gas phase natural gas
US6739131B1 (en) Combustion-driven hydroelectric generating system with closed loop control
US20040088987A1 (en) Integrated gas compressor
US4220009A (en) Power station
CN105840983B (en) A kind of LNG skid-mounted gas feeder
CN101255946B (en) Self-balance method and apparatus for natural gas thermal value at pressure regulating station
US6182615B1 (en) Combustion-driven hydroelectric generating system
Brun et al. Machinery and energy systems for the Hydrogen Economy
CN201526804U (en) Liquid oxygen gasification device specially used for oxygen-richened micro-oil ignition and combustion stabilization device
CN2246235Y (en) Cold micro-pressuring pipeline transport appts. for forming gas
CN2262161Y (en) Gasifying concentrate transport device for light hydrocarbon oil
JPH05502135A (en) fuel cell power generator
CN102095071B (en) Method and device for supplying multifunctional mobile liquid-phase natural gas and gas-phase natural gas
CN1088815C (en) Pentane pipeline liquefied gas device
US12009730B2 (en) Mobile diversified power generation system utilizing gas
CN220981004U (en) High-pressure high-temperature gasification device for liquid carbon dioxide
CN218378972U (en) LNG gas station storage tank pressure boost sled
CN113586942A (en) Multifunctional low-temperature storage tank
CN2162584Y (en) Liquid-gas double-pipe transmission device compound liquid fuel for household
CN2313168Y (en) Water-pressure type safety liquid-fuel gasifying stove
CN2723852Y (en) Liquefied gas supply system of one-house-one storage tank
CN2491715Y (en) Light hydrocarbon fuel gasifier
CN116658298A (en) Liquid oxygen and liquid methane comprehensive utilization system and method

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