CN205603525U - Gaseous synthesizer - Google Patents
Gaseous synthesizer Download PDFInfo
- Publication number
- CN205603525U CN205603525U CN201620443058.8U CN201620443058U CN205603525U CN 205603525 U CN205603525 U CN 205603525U CN 201620443058 U CN201620443058 U CN 201620443058U CN 205603525 U CN205603525 U CN 205603525U
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- Prior art keywords
- gas
- fischer
- reactor
- condenser
- tropsch reactor
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- 239000007788 liquid Substances 0.000 claims abstract description 31
- 238000003786 synthesis reaction Methods 0.000 claims abstract description 31
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 30
- 238000000926 separation method Methods 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 7
- 238000001514 detection method Methods 0.000 claims description 2
- 238000009827 uniform distribution Methods 0.000 claims description 2
- 230000008901 benefit Effects 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000012824 chemical production Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The utility model discloses a gaseous synthesizer, including ft synthesis unit and gas -liquid separation unit, wherein, the ft synthesis unit includes that booster pump, expense hold in the palm reactor, heating device and condenser, and the expense asks reactor to be equipped with the liquefaction catalyst, and heating device sets up and makes progress in the week of holding in the palm the reactor take, the gas -liquid separation unit includes gas -liquid separation ware and tail gas processing apparatus, the exit end and the expense of booster pump ask the top of reactor to be linked together, and the bottom of expense support reactor is linked together with the one end of condenser, and the other end and the vapour and liquid separator of condenser are linked together, and vapour and liquid separator's gas outlet is linked together with tail gas processing apparatus's air inlet. The utility model has the advantages that under the effect of catalyst, carry out ft synthesis under lower temperature and the pressure condition with the gas mixture, generate results such as light oil and combustible gas. This equipment has characteristics such as easy and simple to handle, that the security is high, the energy consumption is low, economic benefits is good.
Description
The technical field is as follows:
the utility model relates to a gas synthesis device, which is suitable for the mixed gas after treatment in chemical production.
Background art:
the current chemical synthesis industry develops rapidly, and the synthetic product relates to all aspects in daily life, but the synthetic process of the chemical industry selects more severe conditions, generally adopts medium pressure or high pressure, and puts forward high requirements on the design and manufacture difficulty and safety of equipment.
The utility model has the following contents:
the to-be-solved problem of the utility model is to provide a gas synthesis device realizes the processing that the mist converts into light oil and combustible gas under the low temperature low pressure condition, is applicable to little to the kilogram rank, big to the multistage refuse treatment of tonnage.
In order to solve the technical problem, the utility model discloses a technical scheme is:
a gas synthesis device comprises a Fischer-Tropsch synthesis unit and a gas-liquid separation unit; wherein,
the Fischer-Tropsch synthesis unit comprises a booster pump, a Fischer-Tropsch reactor, a heating device and a condenser, wherein a liquefaction catalyst is filled in the Fischer-Tropsch reactor, and the heating device is arranged on the circumferential direction of the Fischer-Tropsch reactor;
the gas-liquid separation unit comprises a gas-liquid separator and a tail gas treatment device;
the outlet end of the booster pump is communicated with the top end of the Fischer-Tropsch reactor, the bottom end of the Fischer-Tropsch reactor is communicated with one end of a condenser, the other end of the condenser is communicated with a gas-liquid separator, and a gas outlet of the gas-liquid separator is communicated with a gas inlet of the tail gas treatment device.
The utility model discloses further improvement lies in: the top end of the fischer tropsch reactor is also provided with a pressure gauge.
The utility model discloses further improvement lies in: the top end of the Fischer-Tropsch reactor is also provided with a gas detection meter.
The utility model discloses further improvement lies in: the heating device is a crawler-type heater.
The utility model discloses further improvement lies in: the bottom end of the Fischer-Tropsch reactor is also provided with a gas uniform distribution device.
The utility model discloses further improvement lies in: a back pressure valve is arranged on a pipeline which is communicated with one end of the condenser at the bottom end of the Fischer-Tropsch reactor.
The utility model discloses further improvement lies in: ball valves are arranged at the gas outlet of the gas-liquid separator, the liquid outlet of the gas-liquid separator and the gas outlet of the tail gas treatment device.
Compared with the prior art, the utility model has the advantages that under the effect of catalyst, with the gas mixture carry out the ft synthesis under lower temperature and pressure (for conventional ft synthesis technology) condition, produce products such as light oil and combustible gas. The equipment has the characteristics of simple and convenient operation, high safety, low energy consumption, good economic benefit and the like.
Description of the drawings:
fig. 1 is a schematic diagram of the basic structure of the present invention.
In the figure: the method comprises the following steps of marking 1 as a Fischer-Tropsch synthesis unit, including (101-108); a gas-liquid separation unit is indicated at the beginning of 2 and comprises (201-205).
The specific implementation mode is as follows:
the following detailed description of the embodiments of the present invention will be made with reference to the accompanying drawings.
As shown in figure 1, the gas synthesis treatment equipment comprises a Fischer-Tropsch synthesis unit and a gas-liquid separation unit; the Fischer-Tropsch synthesis unit comprises a booster pump 101, a Fischer-Tropsch reactor 104, a heating device 105 and a condenser 108, wherein the Fischer-Tropsch reactor 104 is internally provided with a liquefaction catalyst, and the heating device 105 is arranged on the circumferential direction of the Fischer-Tropsch reactor 104; the gas-liquid separation unit comprises a gas-liquid separator 201 and a tail gas treatment device 203; the outlet end of the booster pump 101 is communicated with the top end of the Fischer-Tropsch reactor 104, the bottom end of the Fischer-Tropsch reactor 104 is communicated with one end of the condenser 108, the other end of the condenser 108 is communicated with the gas-liquid separator 201, and the gas outlet of the gas-liquid separator 201 is communicated with the gas inlet of the tail gas treatment device 203.
During operation, the mixed gas is synthesized in the Fischer-Tropsch reactor 104 with the liquefaction catalyst to produce short-chain hydrocarbon compounds and harmless gas which can be directly discharged, and then cooled by the condenser 108. The volume of the Fischer-Tropsch reactor 104 was 316L. The Fischer-Tropsch synthesis products passing through the pipeline are separated, liquid flows out through the end of the ball valve 205, and gas enters the tail gas treatment device 203 and is discharged or recycled through the ball valve 204.
Specific embodiments of the Fischer-Tropsch synthesis unit include: the pressure of the mixed gas in the Fischer-Tropsch reactor 104 is increased and maintained to the pressure required by the reaction through a booster pump 101 and a back pressure valve 107, and the pressure is monitored by a pressure gauge 102;
the light oil and combustible gas generated by the Fischer-Tropsch reaction enter a condenser 108 for cooling treatment;
the reaction product after the temperature reduction treatment enters a gas-liquid separator 201 for oil-gas separation, oil substances flow out through a ball valve 205, and gas substances are collected and utilized or discharged after passing through a ball valve 204.
Particularly, the utility model provides a gas synthesizer divide into two big units: a Fischer-Tropsch synthesis unit and a gas-liquid separation unit.
The Fischer-Tropsch synthesis is to pressurize the mixed gas by a booster pump 101 and then enter a Fischer-Tropsch reactor 104 for gas synthesis;
further, in order to ensure that the pressure inside the fischer-tropsch reactor 104 meets the reaction requirement, a back pressure valve 107 meeting the requirement is additionally arranged at a proper position of the gas outlet pipeline to meet the requirement of controlling the pressure; a pressure gauge 102 is arranged at the upper part of the tower body and is used for monitoring the internal pressure;
the fischer-tropsch reactor temperature requirement is accomplished by a track heater heating scheme.
The light oil and combustible gas after Fischer-Tropsch synthesis enter a condenser 108 for cooling;
further, the oil-gas mixture is separated through the gas-liquid separator 201, light oil flows out and is collected at the oil outlet end, and the gas part is emptied or collected and utilized after passing through the tail gas treatment device 203.
Claims (7)
1. A gas synthesis apparatus, characterized by: comprises a Fischer-Tropsch synthesis unit and a gas-liquid separation unit; wherein,
the Fischer-Tropsch synthesis unit comprises a booster pump (101), a Fischer-Tropsch reactor (104), a heating device (105) and a condenser (108), wherein a liquefaction catalyst is arranged in the Fischer-Tropsch reactor (104), and the heating device (105) is arranged on the circumferential direction of the Fischer-Tropsch reactor (104);
the gas-liquid separation unit comprises a gas-liquid separator (201) and a tail gas treatment device (203);
the outlet end of the booster pump (101) is communicated with the top end of the Fischer-Tropsch reactor (104), the bottom end of the Fischer-Tropsch reactor (104) is communicated with one end of a condenser (108), the other end of the condenser (108) is communicated with a gas-liquid separator (201), and the gas outlet of the gas-liquid separator (201) is communicated with the gas inlet of the tail gas treatment device (203).
2. A gas synthesis plant according to claim 1, characterised in that: the top end of the Fischer-Tropsch reactor (104) is also provided with a pressure gauge (102).
3. A gas synthesis plant according to claim 1, characterised in that: the top end of the Fischer-Tropsch reactor (104) is also provided with a gas detection meter (103).
4. A gas synthesis plant according to claim 1, characterised in that: the heating device (105) is a caterpillar heater.
5. A gas synthesis plant according to claim 1, characterised in that: the bottom end of the Fischer-Tropsch reactor (104) is also provided with a gas uniform distribution device (106).
6. A gas synthesis plant according to claim 1, characterised in that: a back pressure valve (107) is arranged on a pipeline which is communicated with one end of the condenser (108) at the bottom end of the Fischer-Tropsch reactor (104).
7. A gas synthesis plant according to claim 1, characterised in that: ball valves are arranged at a gas outlet of the gas-liquid separator (201), a liquid outlet of the gas-liquid separator and an air outlet of the tail gas treatment device (203).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620443058.8U CN205603525U (en) | 2016-05-16 | 2016-05-16 | Gaseous synthesizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620443058.8U CN205603525U (en) | 2016-05-16 | 2016-05-16 | Gaseous synthesizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205603525U true CN205603525U (en) | 2016-09-28 |
Family
ID=56967324
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620443058.8U Active CN205603525U (en) | 2016-05-16 | 2016-05-16 | Gaseous synthesizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205603525U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112781946A (en) * | 2019-11-08 | 2021-05-11 | 国家能源投资集团有限责任公司 | Split-phase collecting device and method for multiphase mixed materials and application of split-phase collecting device and method |
| US11389787B2 (en) | 2019-02-20 | 2022-07-19 | Kara Technologies Inc. | Catalyst structure and method of upgrading hydrocarbons in the presence of the catalyst structure |
| US11725150B2 (en) | 2020-08-18 | 2023-08-15 | Kara Technologies Inc. | Method of light oil desulfurization in the presence of methane containing gas environment and catalyst structure |
| US12006475B2 (en) | 2020-08-26 | 2024-06-11 | Kara Technologies Inc. | Organic solid biomass conversion for liquid fuels/chemicals production in the presence of methane containing gas environment and catalyst structure |
-
2016
- 2016-05-16 CN CN201620443058.8U patent/CN205603525U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11389787B2 (en) | 2019-02-20 | 2022-07-19 | Kara Technologies Inc. | Catalyst structure and method of upgrading hydrocarbons in the presence of the catalyst structure |
| US11833492B2 (en) | 2019-02-20 | 2023-12-05 | Kara Technologies, Inc. | Catalyst structure and method of upgrading hydrocarbons in the presence of the catalyst structure |
| CN112781946A (en) * | 2019-11-08 | 2021-05-11 | 国家能源投资集团有限责任公司 | Split-phase collecting device and method for multiphase mixed materials and application of split-phase collecting device and method |
| CN112781946B (en) * | 2019-11-08 | 2023-09-12 | 国家能源投资集团有限责任公司 | Phase-splitting collecting device and method for multiphase mixed materials and application of phase-splitting collecting device and method |
| US11725150B2 (en) | 2020-08-18 | 2023-08-15 | Kara Technologies Inc. | Method of light oil desulfurization in the presence of methane containing gas environment and catalyst structure |
| US12006475B2 (en) | 2020-08-26 | 2024-06-11 | Kara Technologies Inc. | Organic solid biomass conversion for liquid fuels/chemicals production in the presence of methane containing gas environment and catalyst structure |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |