CN2226189Y - Combined pot apparatus for light hydrocarbon complexing gasifying density control - Google Patents

Combined pot apparatus for light hydrocarbon complexing gasifying density control Download PDF

Info

Publication number
CN2226189Y
CN2226189Y CN 95215406 CN95215406U CN2226189Y CN 2226189 Y CN2226189 Y CN 2226189Y CN 95215406 CN95215406 CN 95215406 CN 95215406 U CN95215406 U CN 95215406U CN 2226189 Y CN2226189 Y CN 2226189Y
Authority
CN
China
Prior art keywords
tank
gasifying
concentration
iii
jar
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 95215406
Other languages
Chinese (zh)
Inventor
李勇
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 95215406 priority Critical patent/CN2226189Y/en
Application granted granted Critical
Publication of CN2226189Y publication Critical patent/CN2226189Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The utility model relates to an integral combined pot apparatus which integrates a primary gasifying pot (A), a secondary gasifying pot (B) and a mixture concentration regulating pot (C). The concentration is regulated by a method that an electric control device and a concentration sensor control the openings degrees of electromagnetic valves (1), (2) and (3).

Description

Dense combined tank device is transferred in the compound gasification of lighter hydrocarbons
The utility model relates to a kind of can the adjustment and stablizes in the mixed gas the compound gasification of light hydrocarbon gas concentration and transfer dense combined tank device.
At present, the existing injection pressurized air that adopts makes the device of light hydrocarbon liquid gasification produce the technology of light hydrocarbon C5 combination gas, with the combination gas after the gasification, directly delivers to the kitchen range burning.The concentration of the combination gas of producing like this is very unstable.Alter a great deal with outside air temperature, and can't adjust, so bad during its firing effect fashion.
The purpose of this utility model exactly in order to overcome the deficiency of prior art basis, provides a kind of energy control to adjust the gasification of made lighter hydrocarbons combination gas concentration, transfer dense composite set.
The purpose of this utility model is achieved in that a pressurized container (jar) is separated with steel plate by 3: 7 volume ratios, wherein account for 70% volume for one gasifying tank account for 30% volume for secondary gasifying tank, in two jars the gasification injection pipe is housed all, have a plurality of jet apertures on the parallel portion tube wall of bottom, the bottom that its position is installed in jar and with parallel at the bottom of the jar.The mixed gas that comes out from the one gasifying tank gas outlet enters the tubular type vaporizer of secondary gasifying tank behind an one way stop peturn valve and a ball valve, the concentration of mixed gas is improved, pass through the setting jar of vertical little volume of welding (be about secondary air tank volume about 1/3) on this jar top mutually, be referred to as mixed concentration adjusted tank.Draw a breathing pipe again from the one gasifying tank air outlet, in valve leads to into this mixed concentration adjusted tank, when need are adjusted mixture strength, only need by electric controller respectively control electromagnetic valve (1), (2), and the aperture of (3) get final product.
Advantage of the present utility model is exactly can arbitrarily adjust and stable concentration of mixing.
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is the section of structure of one of the utility model enforcement.(I) one gasifying tank among Fig. 1, (II) secondary gasifying tank, (III) mixed concentration adjusted tank.Solenoid valve, (2) solenoid valve, (3) solenoid valve and safety check, (4) outer wall, (5) once gas outlet of dividing plate, (6), (7) pressure gauge, (8) one way stop peturn valve, (9) pressure gauge with electric contact, injection pipe once gasifies (10), (11) compressed air inlet pipe, (12) fuel supply line, (13) solenoid valve, (14) pollutant exhaust hole, (15) pollutant exhaust hole, (16) second gasification injection pipe, (17) perpendicular tank wall, (18) outlet total valve, (19) concentration detection sensor.
Jar (I), jar (II) among Fig. 1, separate jar (II), jar (III) orthogonal perforation and be welded into one with dividing plate (5).(11) and valve (8) enter the injection pipe that once gasifies (10) and the liquid light hydrocarbon oil in the jar (I) is sprayed and produce the mixed once combustion gas by the road when pressurized air, this mixed gas enters the second gasification injection pipe (16) of secondary gasifying tank (II) liquid bottom through solenoid valve and safety check (3) again through outlet (6), spray by lighter hydrocarbons jar (III), thereby produce the higher secondary combination gas of concentration, when mixed concentration adjusted tank (III) outlet port gas concentration detect concentration too high than the time, electric control box increases with regard to control valve (2) aperture, and valve (3) aperture reduces.When once the concentration of gas concentration own just exceeded required concentration, electric controller reduced concentration with regard to cut-off valve (3) and open valve (1) advances some air to mixed concentration adjusted tank (III).The one gasifying tank of volume.
In addition, solenoid valve (13) is refueled to jar (II) by jar (I) by fluid level controller control, but lighter hydrocarbons oil level excursion is the ratio ranges of shared volume in jar (II): 20 (low level)~30% (high position).
Pressure gauge with electric contact (9) has been stipulated the upper and lower of pressure range, and the present embodiment regulation is limited to 0.15MPa-0.6MPa up and down.
Present embodiment jar (I) diameter (II) is 1 meter, and the diameter of perpendicular jar (III) is 0.4 meter, and its volume ratio (I): (II): (III) being about 7: 3: 1 steel plate materials is Q235-AF, thickness of slab 8MM, its design pressure 0.60MP working pressure 0.15MP.
Once gasify among Fig. 1 injection pipe (10) and second gasification injection pipe (16) all is to make with seamless steel pipe.And have diameter 2-3 (mm) aperture equably on the steel pipe walls of parallel portion at the bottom of the jar, each cross section is made a call to three and is connected the hole that is mutually 120 ° with the center, 30-60MM between each punching cross section, this pipe least significant end wants seal weld dead.

Claims (1)

1, a kind of can the adjustment stablize in the combination gas the gently compound gasification of lighter hydrocarbons of gas concentration and transfers dense composite set, it is characterized in that: one gasifying tank (I), secondary gasifying tank and (II) mixed mixed concentration adjusted tank (III) three combination make an overall structure, wherein one gasifying tank (I) and secondary gasifying tank (II) are to separate two parts that are split into steel plate in the middle of the tank body, mixed concentration adjusted tank (III) vertically passes through on the top tank skin that is welded on secondary gasifying tank (II) mutually, three's volume ratio (I): (II): (III) about 7: 3: 1.
CN 95215406 1995-06-30 1995-06-30 Combined pot apparatus for light hydrocarbon complexing gasifying density control Expired - Fee Related CN2226189Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 95215406 CN2226189Y (en) 1995-06-30 1995-06-30 Combined pot apparatus for light hydrocarbon complexing gasifying density control

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 95215406 CN2226189Y (en) 1995-06-30 1995-06-30 Combined pot apparatus for light hydrocarbon complexing gasifying density control

Publications (1)

Publication Number Publication Date
CN2226189Y true CN2226189Y (en) 1996-05-01

Family

ID=33864768

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 95215406 Expired - Fee Related CN2226189Y (en) 1995-06-30 1995-06-30 Combined pot apparatus for light hydrocarbon complexing gasifying density control

Country Status (1)

Country Link
CN (1) CN2226189Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1068422C (en) * 1997-03-21 2001-07-11 张慎发 Automatic gasifying pipeline gas supply device for light hydrocarbon fuel
CN107490017A (en) * 2017-09-15 2017-12-19 内蒙古晔路盛燃气工程有限公司 A kind of bubbling carburetors

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1068422C (en) * 1997-03-21 2001-07-11 张慎发 Automatic gasifying pipeline gas supply device for light hydrocarbon fuel
CN107490017A (en) * 2017-09-15 2017-12-19 内蒙古晔路盛燃气工程有限公司 A kind of bubbling carburetors

Similar Documents

Publication Publication Date Title
CN114183242A (en) Ammonia fuel engine supply system
CN2226189Y (en) Combined pot apparatus for light hydrocarbon complexing gasifying density control
CN105298671A (en) Engine micro diesel ignition natural gas equivalent weight air combustion ratio combustion system and control method
CN2422459Y (en) Fuel system of gas-diesel oil double fuel engine
CN212178930U (en) Air and light hydrocarbon mixed gas bubbling gas making device
CN211119465U (en) Gas system
CN211119466U (en) Liquid fuel puffing splitter system for refrigeration and fuel gas
CN211420085U (en) Liquid fuel puffing fission device system for heating
CN206206020U (en) One kind hydrogenation low pressure EGR system
CN217978395U (en) Light hydrocarbon gas making equipment
CN111434914A (en) Hydrogen-containing auxiliary fuel and main fuel high-pressure common rail injection system
CN1102214C (en) Electrothermal water bath type equipment for gasifying pentane
CN212339243U (en) Coaxial nested burner for incineration equipment suitable for treating waste gas air quantity fluctuation
CN202140183U (en) Intelligent electrical-control oil supply system for petrol engine
CN2200117Y (en) Gaseous and liquid fuel universal range
CN206860310U (en) The carburetor of two stroke engine
CN109855111B (en) Gas system
CN201145136Y (en) Liquid gasifying device
CN110194977B (en) Horizontal LNG recondensing device
CN2166907Y (en) High efficiency and energy-saving gas flame cutting device with liquid fuel mixed with oxygen
CN1133522C (en) Jet suction circulating gasification device for cutting welding equipment and cutting torch with said device
CN2517975Y (en) Oil-gas burning pot
CN2380336Y (en) Supersonic gasoline cutting-welding machine
CN2212133Y (en) Fuel continuous service big and small pressure tank
CN2911380Y (en) Rasidual liquid burning aid for LPG 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