CN2644862Y - Novel gasification tank - Google Patents

Novel gasification tank Download PDF

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Publication number
CN2644862Y
CN2644862Y CN 03284004 CN03284004U CN2644862Y CN 2644862 Y CN2644862 Y CN 2644862Y CN 03284004 CN03284004 CN 03284004 CN 03284004 U CN03284004 U CN 03284004U CN 2644862 Y CN2644862 Y CN 2644862Y
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CN
China
Prior art keywords
gasification
tank
tank body
gas
gasification installation
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 03284004
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Chinese (zh)
Inventor
宋胜梅
陈召厚
张淑君
孙勇
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Individual
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Individual
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Publication date
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Priority to CN 03284004 priority Critical patent/CN2644862Y/en
Application granted granted Critical
Publication of CN2644862Y publication Critical patent/CN2644862Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a new-type gasification tank, belonging to a naphtha (Light Hydrocarbon) gasification device technical field. A vertical board is arranged in the tank; a gas-inlet pipe which is communicated with the outside and a gasification device is arranged at one end of the tank; the gasification device comprises two layers of cannula, and a plurality of micro-holes are positioned at the cannula; an anti-static net is fixed on the board and the tank; a gas-outlet pipe is arranged on the other end of the tank, and a filter board is arranged on the lower end of the gas-outlet pipe. The gasification tank is used in the naphtha (Light Hydrocarbon) gasification or the liquefied petroleum gas (LPG) gasification.

Description

A kind of novel gasifying tank
Technical field
The utility model belongs to naphtha gasification installation technical field, particularly a kind of novel gasifying tank that naphtha (lighter hydrocarbons) or liquefied petroleum gas can be gasified totally.
Background technique
Naphtha (lighter hydrocarbons) gasification back being produced inflammable gas, supply with industry and civilian, is one of predominant use of petroleum products, and civilian liquid gas etc. promptly belongs to this.Liquefied petroleum gas in the existing civilian liquefied gas tank reaches the port of kitchen range, fire door or water heater etc. from the outlet port with gaseous state by pipeline, and it is available to light the back.This liquefied gas tank only is used for the can liquefied petroleum gas, tank body itself does not make the function of liquid fuel gasification, the formation of its combustible gas is the gasification by liquefied petroleum gas itself, and in gasification, light molecule oil plant at first gasifies, weight molecule oil plant gasification lags behind, and will occur two kinds of phenomenons like this: the one, and jar PetroChina Company Limited.'s LNG gasifaction initial stage and last gasification change in concentration are bigger; The 2nd, oil molecule proportion changes the variation greatly that causes the white index of inflammable gas China greatly, and liquefied petroleum gas can't be synchronously and all gasifications, causes gasification incomplete and waste.In addition, this gasifying tank only is applicable to liquefied petroleum gas, and can not make other liquid fuel such as gasifications such as light oil, diesel oil, and this is restricted with regard to the source that makes the combustible gas raw material.Also have a kind of gasification steel cylinder, inner employing Buddha's warrior attendant sand body micropore or plastics barred body micropore technology, but its less than one is to use the life-span short, and the 2nd, be easy to generate static, use not too safe.
The model utility content
The purpose of this utility model is to propose a kind of novel gasifying tank that is used for naphtha (lighter hydrocarbons) gasification.
The technical solution of the utility model is: novel gasifying tank comprises tank body 1 (Fig. 1); In jar vertical baffle plate 2 is installed; One end of tank body 1 is provided with and the extraneous suction tude 5 that communicates; Suction tude 5 is communicated with the gasification installation 3 that is installed on jar interior bottom, and gasification installation 3 is made up of bilayer sleeve 8,9, is distributed with micropore 10 (Fig. 2) on the sleeve pipe, and tank body the other end is provided with steam outlet pipe 6; Gasification installation 3 and antistatic net 4 axially are provided with along tank body; Antistatic net 4 is positioned at gasification installation 3 tops, is connected with tank body 1 with baffle plate 2; Steam outlet pipe 6 lower ends are equipped with filter plate 7; Tank body 1 top is provided with the service ports 11 of band sealed door.
Novel gasifying tank gasification: liquid fuel naphtha (lighter hydrocarbons etc.) or liquefied petroleum gas are added in the jar from suction tude 5, send into gas through suction tude 5 pressurizations (being no more than 0.03 kilogram) again, add liquid fuel and in gasification installation 3, collide by the gas molecule that the internal layer micropore enters with suction tude 5, form containing with air molecule, by outer micropore ejection, simultaneously again with other oil plant molecular collision, friction, reach second gasification, form higher gasification concentration, mixed gas after the gasification moves upward, from the mesh of antistatic net 4, pass, cut apart the less particle shape of formation, by deriving the static in the mixed gas being connected of grid and tank body; Mixed gas continues upwards to lead to gas pipeline through steam outlet pipe 6 following filter plates 7 by steam outlet pipe 6, and filter plate 7 is isolated the elaioleucite that drips shape, and further derives the static in the gas.
The gasification installation 3 of novel gasifying tank is positioned at the below of tank body, makes the little liquid fuel of big liquid fuel of molecular weight and molecular weight realize gasification synchronously, and the combustible gas after the gasification keeps stable concentration, and reaches the purpose that is gasified totally; It not only can directly use naphtha (lighter hydrocarbons), makes it to reach 100% gasification, liquefied petroleum gas is reached be gasified totally and does not stay raffinate, has remedied existing liquefied gas tank and can only use liquefied petroleum gas and leave the wasting deficiency of raffinate; The static function of leading of antistatic net 4 and filter screen 7 has been eliminated the generation danger that static brought in the liquid fuel gasification process.The manufacture cost of novel gasifying tank increases few, has but increased the raw material sources of combustible gas, and gasification result also is far superior to existing gasification installation.
Embodiment
Tank body 1 is a long-round-shape, two circular arc (Fig. 1); In jar vertical plate washer 2 is installed; Tank body one end is provided with and the extraneous suction tude 5 that communicates, and is communicated with gasification installation 3; Gasification installation 3 is made up of bilayer sleeve 8,9, is distributed with micropore 10 on the sleeve pipe, is positioned at a jar bottom; Antistatic net 4 is metal net shaped, is fixed on plate washer 2 and the tank body 1, is positioned at the top of gasification installation 3; Gasification installation 3 and antistatic net 4 axially are provided with along tank body; Tank body the other end is provided with steam outlet pipe 6, and its lower end is equipped with filter plate 7; Service ports 11 is positioned at suction port one end.

Claims (2)

1. a novel gasifying tank comprises tank body, it is characterized in that: tank body one end is provided with and the extraneous suction tude that communicates, suction tude is communicated with the gasification installation that is installed on jar interior bottom, gasification installation is made up of bilayer sleeve, is distributed with micropore on the sleeve pipe, and tank body the other end is provided with steam outlet pipe.
2. gasifying tank as claimed in claim 1 is characterized in that: in jar vertical plate washer is installed; Gasification installation and antistatic net axially are provided with along tank body; The antistatic net is positioned at the gasification installation top, is connected with tank body with baffle plate; The steam outlet pipe lower end is equipped with filter plate; Tank body top is provided with the service ports of band sealed door.
CN 03284004 2003-08-08 2003-08-08 Novel gasification tank Expired - Fee Related CN2644862Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 03284004 CN2644862Y (en) 2003-08-08 2003-08-08 Novel gasification tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 03284004 CN2644862Y (en) 2003-08-08 2003-08-08 Novel gasification tank

Publications (1)

Publication Number Publication Date
CN2644862Y true CN2644862Y (en) 2004-09-29

Family

ID=34303645

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 03284004 Expired - Fee Related CN2644862Y (en) 2003-08-08 2003-08-08 Novel gasification tank

Country Status (1)

Country Link
CN (1) CN2644862Y (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100383456C (en) * 2005-04-26 2008-04-23 吴义东 Supplying device of gas burning system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100383456C (en) * 2005-04-26 2008-04-23 吴义东 Supplying device of gas burning system

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20040929

Termination date: 20090908