CN109340559A - A kind of two-stage type gasifier - Google Patents

A kind of two-stage type gasifier Download PDF

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Publication number
CN109340559A
CN109340559A CN201811333870.5A CN201811333870A CN109340559A CN 109340559 A CN109340559 A CN 109340559A CN 201811333870 A CN201811333870 A CN 201811333870A CN 109340559 A CN109340559 A CN 109340559A
Authority
CN
China
Prior art keywords
shell
heat exchange
main heat
exchange chamber
preheating cavity
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
Application number
CN201811333870.5A
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Chinese (zh)
Inventor
安涛
顾善愚
柴启寅
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.)
Dongfeng Commercial Vehicle Co Ltd
Original Assignee
Dongfeng Commercial Vehicle Co Ltd
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 Dongfeng Commercial Vehicle Co Ltd filed Critical Dongfeng Commercial Vehicle Co Ltd
Priority to CN201811333870.5A priority Critical patent/CN109340559A/en
Publication of CN109340559A publication Critical patent/CN109340559A/en
Pending legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C7/00Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02Discharging liquefied gases
    • F17C7/04Discharging liquefied gases with change of state, e.g. vaporisation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/032Hydrocarbons
    • F17C2221/033Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

A kind of two-stage type gasifier, including shell (1), natural gas line (2) are provided in shell (1), the Imported gas (3) and gas outlet (4) at natural gas line (2) both ends are located at shell (1) both ends, partition (5) are provided in shell (1), gasifier shell (1) is divided into two independent preheating cavities (6) and main heat exchange chamber (7) by partition (5), and Imported gas (3) is located at preheating cavity (6) end, Imported gas (4) is located at main heat exchange chamber (7) end, the preheating cavity water inlet (8) and preheating cavity water outlet (9) being connected with preheating cavity (6) are provided on the shell (1) of preheating cavity (6), the main heat exchange chamber water inlet (10) and main heat exchange chamber being connected with main heat exchange chamber (7) are provided on the shell (1) of main heat exchange chamber (7) Water outlet (11).Realization is divided into two-stage and natural gas is gasified and heated.

Description

A kind of two-stage type gasifier
Technical field
The present invention relates to a kind of gasifier, more specifically to a kind of two-stage type gasifier belongs to automobile engine skill Art field.
Background technique
Currently, the extensive use with liquefied natural gas on vehicle, component capabilities in feed system increasingly by To concern, gasifier is exactly one of critical component.Gasifier is to hand over -162 DEG C of ultralow temperature liquified natural gas through overheat Ventilation formation gas, and it is heated to the device of certain temperature, heat exchange medium is engine coolant.
Since natural gas temperature is too low, causes the heat exchanger in gasifier that can only take co-current mode, prevent coolant liquid Crystallization even freezes;But the heat exchanger effectiveness of downstream heat transfer is relatively low, gasification rate is slow, is not able to satisfy engine and suddenly accelerates Operating condition.
Summary of the invention
It is an object of the invention to can only take heat existing for co-current mode for the heat exchanger in existing gasifier The defects of exchange efficiency is relatively low, gasification rate is slow provides a kind of two-stage type gasifier.
To achieve the above object, the technical solution of the invention is as follows: a kind of two-stage type gasifier, including shell, described Shell in be provided with natural gas line, the Imported gas and gas outlet at natural gas line both ends are located at shell two It holds, is provided with partition in shell, gasifier shell is divided into two independent preheating cavities and main heat exchange chamber, and day by the partition Right gas import is located at preheating cavity end, and Imported gas is located at main heat exchange chamber end, is provided with and preheats on the shell of the preheating cavity The preheating cavity water inlet and preheating cavity water outlet that chamber is connected are provided on the shell of the main heat exchange chamber and are connected with main heat exchange chamber Logical main heat exchange chamber water inlet and main heat exchange chamber water outlet.
Compared with prior art, the beneficial effects of the present invention are:
The present invention includes two heat exchange cavitys of preheating cavity and main heat exchange chamber, and preheating cavity is using co-current mode to natural gas liquid Body is preheated, preliminary to complete gasification;Main heat exchange chamber then uses counter-flow pattern to heat cryogenic natural gas, is rapidly completed Cryogenic gas heating;Therefore the requirement of gasification rate and temperature rise is able to satisfy when suddenly accelerating.
Detailed description of the invention
Fig. 1 is schematic structural view of the invention.
Fig. 2 is perspective view of the present invention.
In figure: shell 1, natural gas line 2, Imported gas 3, gas outlet 4, partition 5, preheating cavity 6, main heat exchange chamber 7, preheating cavity water inlet 8, preheating cavity water outlet 9, main heat exchange chamber water inlet 10, main heat exchange chamber water outlet 11.
Specific embodiment
Below in conjunction with Detailed description of the invention and specific embodiment, the present invention is described in further detail.
Referring to Fig. 1 to Fig. 2, a kind of two-stage type gasifier belongs to a kind of liquefied natural gas gasifying device, including shell 1.Institute Natural gas line 2 is provided in the shell 1 stated, the Imported gas 3 and gas outlet 4 at 2 both ends of natural gas line distinguish position In 1 both ends of shell.
Referring to Fig. 1 to Fig. 2, partition 5 is provided in shell 1, gasifier shell 1 is divided into two independences by the partition 5 Preheating cavity 6 and main heat exchange chamber 7;And Imported gas 3 is located at 6 end of preheating cavity, Imported gas 4 is located at 7 end of main heat exchange chamber.Institute State the preheating cavity water inlet 8 and preheating cavity water outlet 9 for being provided on the shell 1 of preheating cavity 6 and being connected with preheating cavity 6, the master The main heat exchange chamber water inlet 10 and main heat exchange chamber water outlet 11 being connected with main heat exchange chamber 7 are provided on the shell 1 of heat exchanging chamber 7.
Referring to Fig. 1 to Fig. 2, when engine is run, natural gas is entered by Imported gas 3, flows to the another of natural gas line 2 One end, and engine aspirating system is flowed out to through gas outlet 4.Water flow is respectively by the preheating cavity water inlet 8 of preheating cavity 6 and master The main heat exchange chamber water inlet 10 of heat exchanging chamber 7 enters preheating cavity 6 and main heat exchange chamber 7, after completing heat exchange with natural gas, then respectively from The preheating cavity water outlet 9 of preheating cavity 6 and the main heat exchange chamber water outlet 11 of main heat exchange chamber 7 flow out.To complete entire heat exchange Journey.In the process, the water (flow) direction of preheating cavity 6 is consistent with natural gas flow direction, is downstream heat transfer, makes liquified natural gas gas Guarantee that coolant liquid will not be freezed while change;The water (flow) direction of main heat exchange chamber 7 is contrary with natural gas flow, changes for adverse current Heat, heat exchange efficiency are higher than co-current mode, accelerate gasification rate and natural gas temperature rise, and realization is divided into two-stage and gasifies to natural gas And heating, it had not only improved heat exchanger effectiveness but also had effectively prevented the risk that coolant liquid crystallization even freezes.
The above content is a further detailed description of the present invention in conjunction with specific preferred embodiments, and it cannot be said that Specific implementation of the invention is only limited to these instructions.For those of ordinary skill in the art to which the present invention belongs, exist Under the premise of not departing from present inventive concept, a number of simple deductions or replacements can also be made, and above structure all shall be regarded as belonging to Protection scope of the present invention.

Claims (1)

1. a kind of two-stage type gasifier, it is characterised in that: including shell (1), be provided with natural gas line in the shell (1) (2), the Imported gas (3) and gas outlet (4) at natural gas line (2) both ends are located at shell (1) both ends, shell (1) it is provided with partition (5) in, gasifier shell (1) is divided into two independent preheating cavities (6) with the partition (5) and master changes Hot chamber (7), and Imported gas (3) is located at preheating cavity (6) end, Imported gas (4) is located at main heat exchange chamber (7) end, described pre- The preheating cavity water inlet (8) and preheating cavity water outlet (9) being connected with preheating cavity (6) are provided on the shell (1) of hot chamber (6), It is provided with the main heat exchange chamber water inlet (10) being connected with main heat exchange chamber (7) on the shell (1) of the main heat exchange chamber (7) and master changes Hot chamber water outlet (11).
CN201811333870.5A 2018-11-09 2018-11-09 A kind of two-stage type gasifier Pending CN109340559A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811333870.5A CN109340559A (en) 2018-11-09 2018-11-09 A kind of two-stage type gasifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811333870.5A CN109340559A (en) 2018-11-09 2018-11-09 A kind of two-stage type gasifier

Publications (1)

Publication Number Publication Date
CN109340559A true CN109340559A (en) 2019-02-15

Family

ID=65314386

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811333870.5A Pending CN109340559A (en) 2018-11-09 2018-11-09 A kind of two-stage type gasifier

Country Status (1)

Country Link
CN (1) CN109340559A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1148429A (en) * 1994-05-09 1997-04-23 克瓦纳尔工程有限公司 Heat exchanger
CN1800765A (en) * 2005-12-31 2006-07-12 西安华广电站锅炉有限公司 High-efficiency energy-saving modular chamber type heat exchanger
CN202614038U (en) * 2012-04-26 2012-12-19 广州众信实业有限公司 Tubular heat exchanger
CN202770265U (en) * 2012-08-22 2013-03-06 华北电力大学 Natural circulation heat exchanger for supercritical water reactor waste heat removing
CN105423796A (en) * 2014-04-16 2016-03-23 英瑞美国有限责任公司 Counterflow helical heat exchanger
CN106287212A (en) * 2015-05-14 2017-01-04 浙江盾安人工环境股份有限公司 A kind of back-heating type gasifier
CN206131842U (en) * 2016-10-19 2017-04-26 天津瑞岭化工有限公司 In same direction as against current parallelly connected heat exchanger

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1148429A (en) * 1994-05-09 1997-04-23 克瓦纳尔工程有限公司 Heat exchanger
CN1800765A (en) * 2005-12-31 2006-07-12 西安华广电站锅炉有限公司 High-efficiency energy-saving modular chamber type heat exchanger
CN202614038U (en) * 2012-04-26 2012-12-19 广州众信实业有限公司 Tubular heat exchanger
CN202770265U (en) * 2012-08-22 2013-03-06 华北电力大学 Natural circulation heat exchanger for supercritical water reactor waste heat removing
CN105423796A (en) * 2014-04-16 2016-03-23 英瑞美国有限责任公司 Counterflow helical heat exchanger
CN106287212A (en) * 2015-05-14 2017-01-04 浙江盾安人工环境股份有限公司 A kind of back-heating type gasifier
CN206131842U (en) * 2016-10-19 2017-04-26 天津瑞岭化工有限公司 In same direction as against current parallelly connected heat exchanger

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Application publication date: 20190215