CN104109552B - Biomass synthesis gas rotary diesel oil synthesis device - Google Patents

Biomass synthesis gas rotary diesel oil synthesis device Download PDF

Info

Publication number
CN104109552B
CN104109552B CN201410297920.4A CN201410297920A CN104109552B CN 104109552 B CN104109552 B CN 104109552B CN 201410297920 A CN201410297920 A CN 201410297920A CN 104109552 B CN104109552 B CN 104109552B
Authority
CN
China
Prior art keywords
synthesis gas
diesel
biomass
rotating shaft
packed bed
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.)
Active
Application number
CN201410297920.4A
Other languages
Chinese (zh)
Other versions
CN104109552A (en
Inventor
赵山山
梁世明
赵一简
黎晓
谢雪宁
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.)
Huang Yu
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 CN201410297920.4A priority Critical patent/CN104109552B/en
Publication of CN104109552A publication Critical patent/CN104109552A/en
Application granted granted Critical
Publication of CN104109552B publication Critical patent/CN104109552B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

The invention discloses a device for synthesizing diesel oil by cyclone rotation of biomass synthesis gas, which comprises a machine body and a packed bed, wherein a synthesis gas inlet is formed in the machine body, a diesel oil outlet is formed in the lower part of the machine body, a waste gas outlet is formed in the upper part of the right side of the machine body, a motor horizontally connected with a rotating shaft through a coupler is arranged in the middle of the left side of the machine body, and the packed bed is arranged in the machine body and is annularly connected with the rotating shaft. The invention has the outstanding advantages of small occupied area, small space, simple and convenient operation, high production strength and the like.

Description

一种生物质合成气旋转合成柴油装置A Biomass Syngas Rotary Synthetic Diesel Device

技术领域 technical field

本发明涉及一种生物质合成气旋转合成柴油装置,具体地说是涉及一种利用旋转离心器,在离心力环境和催化剂作用下,进行费托合成反应合成柴油的装置。 The invention relates to a device for synthesizing diesel by rotating biomass synthesis gas, in particular to a device for synthesizing diesel by Fischer-Tropsch synthesis reaction using a rotating centrifuge under the action of a centrifugal force environment and a catalyst.

背景技术 Background technique

目前,在生物质合成气制取液体燃料中,均采用费托合成法。费托合成反应已有80余年历史。近年来,能源的可持续性和化石产品的环保问题已经日益明显,发展和推广环保的生物质能源受到各国的重视,生物质原料通过费托合成反应制备液体燃料或高附加值化学品的途径已经获得广泛认可。但传统的费托合成产物主要为直链烷烃、烯烃、少量芳烃和醛醇,产物组成复杂。轻质液体烃少,其产品选择性较差,除重碳烃类可取得较高的选择性外,其它产物的选择性均不高。而采用不同类型的反应器,如固定床、流化床或浆态床,对费托合成产物的选择性几乎没有影响。 At present, the Fischer-Tropsch synthesis method is used in the production of liquid fuels from biomass synthesis gas. Fischer-Tropsch synthesis has a history of more than 80 years. In recent years, the sustainability of energy and the environmental protection of fossil products have become more and more obvious. The development and promotion of environmentally friendly biomass energy has attracted the attention of various countries. Biomass raw materials can be used to prepare liquid fuels or high value-added chemicals through Fischer-Tropsch synthesis. has been widely recognized. However, the traditional Fischer-Tropsch synthesis products are mainly linear alkanes, olefins, a small amount of aromatics and aldols, and the product composition is complex. There are few light liquid hydrocarbons, and their product selectivity is poor. Except for heavy carbon hydrocarbons, which can achieve high selectivity, the selectivity of other products is not high. The use of different types of reactors, such as fixed bed, fluidized bed or slurry bed, has little effect on the selectivity of Fischer-Tropsch synthesis products.

发明内容 Contents of the invention

本发明要解决的技术问题是提供一种利用离心装置进行费托合成反应将生物质合成气在离心力环境和催化剂的共同作用下选择合成柴油的生物质合成气旋转合成柴油装置。 The technical problem to be solved by the present invention is to provide a rotary biodiesel synthesis device using a centrifugal device for Fischer-Tropsch synthesis to select biomass synthesis gas to synthesize diesel under the combined action of a centrifugal force environment and a catalyst.

为了解决上述技术问题,本发明采取以下技术方案: In order to solve the above technical problems, the present invention takes the following technical solutions:

一种生物质合成气旋转合成柴油装置,包括机体和填料床,机体上开设有合成气进口,机体下开设有柴油出口,机体右侧上方设有废气出口,机体左侧中部居中位置设置有通过耦合器与转动轴水平连接的电动机,填料床设置于机体内部并与转动轴环形连接。 A biomass synthesis gas rotary synthetic diesel device, including a body and a packing bed, a synthesis gas inlet is opened on the body, a diesel outlet is opened under the body, an exhaust gas outlet is arranged on the upper right side of the body, and a passageway is set in the middle of the left side of the body The coupler is horizontally connected to the motor with the rotating shaft, and the packing bed is arranged inside the machine body and connected with the rotating shaft in a ring.

所述填料床位于机体部,通过转动轴可环形转动。 The packing bed is located at the body part and can rotate circularly through the rotating shaft.

所述机体可以是圆柱形、方柱形或其它的形状。 The body can be cylindrical, square column or other shapes.

本发明的生物质合成气旋转合成柴油装置具有占地面积小、空间小,操作简易、方便,生产强度大等突出优点。 The biomass synthesis gas rotary synthesis diesel device of the present invention has outstanding advantages such as small footprint, small space, simple and convenient operation, and high production intensity.

附图说明 Description of drawings

图1为本发明剖面结构示意图。 Fig. 1 is a schematic cross-sectional structure diagram of the present invention.

图中名称序号为: The serial numbers in the figure are:

机体1、填料床2、合成气进口3、柴油出口4、废气出口5、电动机6、耦合器7、转动轴8。 Body 1, packing bed 2, syngas inlet 3, diesel outlet 4, exhaust gas outlet 5, electric motor 6, coupler 7, rotating shaft 8.

具体实施方式 detailed description

为了更加详细的介绍本发明,下面结合附图对本发明作进一步的描述。 In order to introduce the present invention in more detail, the present invention will be further described below in conjunction with the accompanying drawings.

如图1所示,一种生物质合成气旋转合成柴油装置,包括机体1和填料床2,机体1上开设有合成气进口3,机体1下开设有柴油出口4,机体1右侧上方设有废气出口5,机体1左侧中部居中位置设置有通过耦合器7与转动轴8水平连接的电动机6,填料床2设置于机体1内部并与转动轴8环形连接。 As shown in Figure 1, a biomass synthesis gas rotary synthetic diesel device includes a body 1 and a packed bed 2, a synthesis gas inlet 3 is provided on the body 1, a diesel outlet 4 is provided under the body 1, and a diesel outlet 4 is provided on the upper right side of the body 1. There is an exhaust gas outlet 5, and a motor 6 horizontally connected to the rotating shaft 8 through a coupler 7 is arranged at the center of the left side of the body 1. The packing bed 2 is arranged inside the body 1 and is connected to the rotating shaft 8 in a ring.

所述填料床2位于机体1内部,通过转动轴8可环形转动。 The packing bed 2 is located inside the machine body 1 and can rotate circularly through a rotating shaft 8 .

所述机体1可以是圆柱形、方柱形或其它的形状。 The body 1 can be cylindrical, square column or other shapes.

本发明的具体操作方法如下: Concrete operation method of the present invention is as follows:

将费托合成反应的鈷基或铁基催化剂放置在装置的填料床2内,启动电动机6,催化剂填料床2处于旋转状态,生物质合成气由位于机体1上方的合成气进口3进入,合成气通过高速旋转的催化剂填料床2发生费托合成反应,生成的产物以柴油为主的烃类,在离心力作用下迅速离开填料床2,由柴油出口(4)排出。 The cobalt-based or iron-based catalyst for the Fischer-Tropsch synthesis reaction is placed in the packed bed 2 of the device, the motor 6 is started, the catalyst packed bed 2 is in a rotating state, and the biomass synthesis gas enters from the synthesis gas inlet 3 located above the body 1 to synthesize Gas passes through the high-speed rotating catalyst packed bed 2 to undergo a Fischer-Tropsch synthesis reaction, and the produced products are mainly diesel oil, which quickly leaves the packed bed 2 under the action of centrifugal force and is discharged from the diesel outlet (4).

合成气流速和不同的离心力影响CO转化率,最佳的反应温度为210~320℃;最佳的反应压力为1~2MPa。 Synthetic gas flow rate and different centrifugal forces affect the conversion rate of CO. The optimum reaction temperature is 210-320°C; the optimum reaction pressure is 1-2MPa.

以上所述并非是对本发明的限定,在不脱离本发明的创造构思的前提下,任何显而易见的替换均在本发明的保护范围之内。 The above description is not a limitation of the present invention, and any obvious replacements are within the protection scope of the present invention without departing from the inventive concept of the present invention.

Claims (1)

1.一种生物质合成气旋转合成柴油的方法,其特征在于:所述的生物质合成气旋转合成柴油的方法的步骤如下: 1. a kind of method that biomass synthesis gas rotates synthetic diesel oil, it is characterized in that: the step of the method for the rotation synthesis diesel of described biomass synthesis gas is as follows: 将费托合成反应的钴基或铁基催化剂放置在装置的填料床(2)内,启动电动机(6),催化剂填料床(2)处于旋转状态,生物质合成气由位于机体(1)上方的合成气进口(3)进入,合成气通过高速旋转的催化剂填料床(2)发生费托合成反应,生成的产物以柴油为主的烃类,在离心力作用下迅速离开填料床(2),由柴油出口(4)排出; Place the cobalt-based or iron-based catalyst for the Fischer-Tropsch synthesis reaction in the packed bed (2) of the device, start the motor (6), the catalyst packed bed (2) is in a rotating state, and the biomass synthesis gas is located above the body (1) The synthesis gas inlet (3) enters, and the synthesis gas passes through the high-speed rotating catalyst packed bed (2) to undergo a Fischer-Tropsch synthesis reaction, and the produced products are mainly diesel hydrocarbons, which quickly leave the packed bed (2) under the action of centrifugal force. Discharged from the diesel outlet (4); 所述生物质合成气流速和不同的离心力影响CO转化率,反应温度为210~320℃;反应压力为1~2Mpa; The biomass synthesis gas flow rate and different centrifugal forces affect the CO conversion rate, and the reaction temperature is 210-320°C; the reaction pressure is 1-2Mpa; 采用的装置包括机体(1)和填料床(2),机体(1)上开设有合成气进口(3),机体(1)下开设有柴油出口(4),机体(1)右侧上方设有废气出口(5),机体(1)左侧中部居中位置设有通过耦合器(7)与转动轴(8)水平连接的电动机(6),填料床(2)设置于机体(1)内部并与转动轴(8)环形连接;所述填料床(2)位于机体(1)内部,通过转动轴(8)可环形转动; The device used includes a body (1) and a packing bed (2). The body (1) is provided with a synthesis gas inlet (3), the body (1) is provided with a diesel outlet (4), and the body (1) is provided with a There is an exhaust gas outlet (5), a motor (6) horizontally connected to the rotating shaft (8) through a coupler (7) is installed in the middle of the left side of the body (1), and the packing bed (2) is arranged inside the body (1) And it is annularly connected with the rotating shaft (8); the packing bed (2) is located inside the machine body (1), and can be rotated annularly through the rotating shaft (8); 所述机体(1)可以是圆柱形方柱形。 The body (1) can be cylindrical or square.
CN201410297920.4A 2014-06-30 2014-06-30 Biomass synthesis gas rotary diesel oil synthesis device Active CN104109552B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410297920.4A CN104109552B (en) 2014-06-30 2014-06-30 Biomass synthesis gas rotary diesel oil synthesis device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410297920.4A CN104109552B (en) 2014-06-30 2014-06-30 Biomass synthesis gas rotary diesel oil synthesis device

Publications (2)

Publication Number Publication Date
CN104109552A CN104109552A (en) 2014-10-22
CN104109552B true CN104109552B (en) 2016-02-24

Family

ID=51706545

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410297920.4A Active CN104109552B (en) 2014-06-30 2014-06-30 Biomass synthesis gas rotary diesel oil synthesis device

Country Status (1)

Country Link
CN (1) CN104109552B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102504858A (en) * 2011-11-10 2012-06-20 北京化工大学 Method for directionally synthesizing gasoline or diesel oil through Fischer-Tropsch process
CN102559234A (en) * 2010-12-21 2012-07-11 北京化工大学 A method for selectively regulating Fischer-Tropsch synthesis products
CN204079898U (en) * 2014-06-30 2015-01-07 赵山山 Biomass synthesis gas rotary diesel oil synthesis device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102559234A (en) * 2010-12-21 2012-07-11 北京化工大学 A method for selectively regulating Fischer-Tropsch synthesis products
CN102504858A (en) * 2011-11-10 2012-06-20 北京化工大学 Method for directionally synthesizing gasoline or diesel oil through Fischer-Tropsch process
CN204079898U (en) * 2014-06-30 2015-01-07 赵山山 Biomass synthesis gas rotary diesel oil synthesis device

Also Published As

Publication number Publication date
CN104109552A (en) 2014-10-22

Similar Documents

Publication Publication Date Title
CN105080436B (en) A kind of ultrasonic wave-coupled high gravity rotating packed bed and its application
CA2956253C (en) Process and rotary machine type reactor
RU2008147899A (en) METHOD FOR CONVERSION OF BIOMASS IN LIQUID FUEL AND SPECIAL CHEMICALS
CN102026716B (en) High shear rotary fixed bed reactor
CN101113348B (en) Process for preparing bio-fuel by high-pressure fluid transformation technique
US8980143B2 (en) Biomass and waste plastics depolymerization machine and methods via supercritical water
CN104059682B (en) Biomass by selective pyrolysis-step transforms device and the method for preparing Aviation Fuel
BRPI1100583A2 (en) hydroliquefaction process directing biomass, comprising two steps of boiling layer hydroconversion
WO2013143243A1 (en) Hypergravity rotating packed bed catalytic reactor and application thereof for modulating distribution of fischer-tropsch process synthetic product
Liu et al. Recyclable Zr/Hf-containing acid-base bifunctional catalysts for hydrogen transfer upgrading of biofuranics: A review
CN102553343B (en) Method and device for continuously separating catalyst of synthetic fluid fuel in slurry bed from product
CN204079898U (en) Biomass synthesis gas rotary diesel oil synthesis device
CN104109552B (en) Biomass synthesis gas rotary diesel oil synthesis device
CN102504858B (en) Method for directionally synthesizing gasoline or diesel oil through Fischer-Tropsch process
CN101215213B (en) A kind of method of supercritical Fischer-Tropsch synthesis
CN107345147A (en) A kind of method that oily sludge prepares high content aromatic product
WO2013067834A1 (en) Method for synthesizing synthesis gas into mixed alcohol
Amrute et al. Catalytic reactions in ball mills
CN101275080A (en) A Fischer-Tropsch synthesis reaction process based on a fixed-bed reactor
CN206385087U (en) A kind of device of the single benzene ring type compounds of biomass pyrolytic volatile matter hydrogenation refining
CN205011701U (en) Novel rotatory awl reaction device
RU96023U1 (en) MULTI-STAGE CENTRIFUGAL EXTRACTOR
KR101776927B1 (en) Synthetic fuel containing high Diesel fuel and gasoline using slurry bubble column reactor
AU2020231195B2 (en) Heat transfer system
CN102442872A (en) Method for directly synthesizing low-carbon olefin by using synthesis gas

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
EE01 Entry into force of recordation of patent licensing contract

Application publication date: 20141022

Assignee: Guangxi mountain hill science and Technology Development Co.,Ltd.

Assignor: Zhao Shanshan

Contract record no.: 2017450000010

Denomination of invention: Rotating device for synthesizing diesel oil by using biomass synthetic gas

Granted publication date: 20160224

License type: Common License

Record date: 20170613

EE01 Entry into force of recordation of patent licensing contract
TR01 Transfer of patent right

Effective date of registration: 20181129

Address after: 530304 Li Xiaozhuan, Hengzhou Zhenjiang Binxi Road, Hengxian Science and Technology Bureau, Nanning City, Guangxi Zhuang Autonomous Region

Patentee after: Guangxi mountain hill science and Technology Development Co.,Ltd.

Address before: 530304 Li Xiaozhuan, Hengzhou Zhenjiang Binxi Road, Hengxian Science and Technology Bureau, Nanning City, Guangxi Zhuang Autonomous Region

Patentee before: Zhao Shanshan

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20250724

Address after: Room C202, Building 8, Free Bay, Ronghe Shanshui Meidi Group 3, No. 155 Minzu Avenue, Qingxiu District, Nanning City, Guangxi Zhuang Autonomous Region 530012

Patentee after: Huang Yu

Country or region after: China

Address before: 530304 Li Xiaozhuan, Hengzhou Zhenjiang Binxi Road, Hengxian Science and Technology Bureau, Nanning City, Guangxi Zhuang Autonomous Region

Patentee before: Guangxi mountain hill science and Technology Development Co.,Ltd.

Country or region before: China

TR01 Transfer of patent right