METHOD AND APPARATUS FOR COMPRESSION OF AMMONIA SYNTHESIS GAS AND RECYCLE GAS FOR THE PRODUCTION OF AMMONIA BY SCREW COMPRESSORS

Abstract

A method for producing ammonia may be provided. The method may include supplying ammonia synthesis gas to a synthesis gas screw compressor and compressing the synthesis gas. The compressed synthesis gas may be joined with a flow of recycle gas compressed in a recycle gas screw compressor. The compressed combined flow may then be introduced to an ammonia reactor. The ammonia reactor may discharge ammonia, purge gas, and unconverted gas, which may be the recycle gas.

Claims

1. A system for producing ammonia comprising: at least one screw compressor; and an ammonia reactor, wherein the at least one screw compressor compresses at least one of ammonia synthesis gas and recycle gas and supplies a compressed gas flow to the ammonia reactor, and wherein the ammonia reactor discharges produced ammonia, purge gas, and recycle gas.

2. The system of claim 1, comprising one screw compressor configured to receive and compress ammonia synthesis gas and recycle gas, and supply a compressed flow of combined synthesis gas and recycle gas to the ammonia reactor.

3. The system of claim 1, comprising a first screw compressor configured to receive ammonia synthesis gas and discharge a flow of compressed ammonia synthesis gas and a second screw compressor configured to receive recycle gas and discharge a flow of compressed recycle gas, wherein the flows of compressed synthesis gas and compressed recycle gas are combined and supplied to the ammonia reactor.

4. The system of claim 3, wherein the first screw compressor and the second screw compressor are disposed on a single shaft.

5. The system of claim 3, wherein the first screw compressor and the second screw compressor are disposed on separate shafts.

6. The of claim 1, wherein the ammonia reactor is configured to supply the recycle gas to the at least one screw compressor.

7. A method for producing ammonia comprising: supplying ammonia synthesis gas to a screw compressor; compressing the ammonia synthesis gas in the screw compressor; discharging a flow of compressed ammonia synthesis gas; combining a flow of compressed recycle gas with the flow of compressed ammonia synthesis gas, forming a compressed combined gas flow; supplying the compressed combined gas flow to an ammonia reactor, wherein the ammonia reactor discharges a produced ammonia, purge gas, and recycle gas; supplying the recycle gas to a screw compressor; compressing the recycle gas; and supplying the compressed recycle gas to the flow of compressed ammonia synthesis gas.

8. The method of claim 7, wherein the synthesis gas and recycle gas are compressed in a single screw compressor.

9. The method of claim 7, further comprising a first screw compressor and a second screw compressor, wherein the synthesis gas is compressed in a first screw compressor and the recycle gas is compressed in a second screw compressor.

10. The method of claim 9, wherein the synthesis gas screw compressor and recycle gas screw compressor are disposed on a single shaft.

11. The method of claim 9, wherein the synthesis gas screw compressor and recycle gas screw compressor are disposed on separate shafts.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0023] FIG. 1 shows an exemplary block flow chart configuration for the compression of ammonia synthesis gas and recycle gas for the production of ammonia by screw compressors.

[0024] FIG. 2 shows another exemplary block flow chart configuration for the compression of ammonia synthesis gas and recycle gas for the production of ammonia by screw compressors.

[0025] FIG. 3 shows another exemplary block flow chart configuration for the compression of ammonia synthesis gas and recycle gas for the production of ammonia by screw compressors.

DETAILED DESCRIPTION OF THE INVENTION

[0026] Aspects of the invention are disclosed in the following description and related drawings directed to specific embodiments of the invention. Alternate embodiments may be devised without departing from the spirit or the scope of the invention. Additionally, well-known elements of exemplary embodiments of the invention will not be described in detail or will be omitted so as not to obscure the relevant details of the invention. Further, to facilitate an understanding of the description discussion of several terms used herein follows.

[0027] As used herein, the word exemplary means serving as an example, instance or illustration. The embodiments described herein are not limiting, but rather are exemplary only. It should be understood that the described embodiments are not necessarily to be construed as preferred or advantageous over other embodiments. Moreover, the terms embodiments of the invention, embodiments or invention do not require that all embodiments of the invention include the discussed feature, advantage or mode of operation.

[0028] According to the present invention, the use of screw compressors compressing to 120 bar may be utilized, which has never been used for the compression of synthesis gas and the recycle gas. This enables the utilization of the waste heat from the synthesis gas plant and with a conventional methane reformer system leads to a gas consumption of 30 MMBTU/metric ton of ammonia. With improved designs in the reformer section, the utilization of the screw compressors as detailed herein, and low cost skid assembly, the capital cost can be matched pro-rata to a larger plant.

[0029] According to an exemplary embodiment, a method may be provided for compressing pure ammonia synthesis gas N2+3H2, or with limited content of methane and inert gases and recycle gas, by a screw compressor. The synthesis gas screw compressor compressing ammonia synthesis gas with a pressure of between 20 bar and 50 bar, with a volume limited to 60,000 standard cubic meters per hour up to 120 bar discharge pressure, according to the block flow drawing.

[0030] Now referring to exemplary FIG. 1, ammonia synthesis gas 102, N2+3H2, may be supplied to a synthesis gas screw compressor 110. The synthesis gas 102 (syngas) may have the stoichiometric volumes of nitrogen and hydrogen for ammonia synthesis and may have small amounts of impurities such as inert gases and methane. In some exemplary embodiments, the syngas may be in the near molar proportions of 1:3. The ammonia synthesis gas 102 may be supplied with an inlet pressure of 20 bar to 50 bar, depending on the synthesis gas process adopted. The synthesis gas screw compressor 110 may compress the ammonia synthesis gas 102 and discharge compressed ammonia synthesis gas 104. The synthesis gas screw compressor 110 may discharge the compressed ammonia synthesis gas 104 with a pressure of 70 bar to 120 bar. According to some exemplary embodiments, the synthesis gas screw compressor 110 may be a single stage oil-flooded screw gas compressor driven by an electric motor or steam turbine.

[0031] Upon discharge from the synthesis gas screw compressor 110, the compressed ammonia synthesis gas 104 may be joined by recycle gas 122 from a recycle screw compressor 120 forming gas flow 108. The recycle gas 122 may have a pressure of 76 bar to 116 bar. The combined gas flow 108 may flow to an ammonia synthesis reactor 130, which may operate at a pressure of 70 bar to 120 bar. Partial conversion of the combined gas flow 108 to ammonia may occur. Unconverted gas portions 132 may pass to the recycle screw compressor 120. The unconverted gas portions 132 may have a pressure of 66 bar to 116 bar when passed to the recycle screw compressor 120. The recycle screw compressor 120 may compress the unconverted gas 132 and introduce compressed unconverted recycle gas 122 to the compressed ammonia synthesis gas flow 104 from the synthesis gas screw compressor 110 before returning to the ammonia synthesis reactor 130. The recycle screw compressor 120 may be driven by an electric motor or steam turbine and may compress the recycle gas to a pressure of 76-116 bar, as noted above, for blending with the already compressed syngas. The ammonia synthesis reactor 130 may also discharge ammonia product 134 and purge-gas (not shown), which may be separated to recover hydrogen or which may be sent for fuel use. The ammonia product 134 may be sent to the user or to ammonia storage.

[0032] In some embodiments, the ammonia synthesis reactor 130 may be a conventional single or multi-pass converter using one or more magnetite catalyst or using one or more noble metal catalyst based on ruthenium, U.S. Pat. No. 9,150,423 to Hosono et al. The ammonia synthesis reactor 130 may further include a waste heat boiler and an ammonia condenser having any mechanical or chemical system capable of more selectively separating ammonia from a gas mixture including at least hydrogen and nitrogen, as would be understood by a person having ordinary skill in the art. The ammonia condenser may include one or more cryogenic purifiers, including one or more refrigeration exchangers and one or more refrigeration compressors. U.S. Pat. No. 8,926,909 to Filippi et al. describes a method for modernizing the ammonia synthesis loop.

[0033] The above referenced screw compressors may be in one of three configurations, as single units, both units on one driver shaft, or as one unit combining both functions. The method may further lead to the utilization of spare heat from a conventional steam reformer and partial oxidation synthesis gas preparation units, which may provide high energy efficiency and low capital cost.

[0034] Now referring to exemplary FIG. 2, a system utilizing a synthesis gas compressor and recycle gas compressor in series may be disclosed. In some embodiments, the screw compressors may be disposed on a single drive shaft. As in the system and process shown in FIG. 1, syngas 202 may be provided to a syngas compressor 210. Recycle gas 232 may be supplied to a recycle gas compressor 220 on the same drive shaft as syngas compressor 210, where recycle gas 232 may be compressed. The compressed syngas 204 may bypass the recycle gas compressor 220 and be introduced and combined with the compressed recycle gas 222 forming compressed gas flow 208, which may be introduced to an ammonia synthesis reactor 230. The synthesis gas compressor 210 and the recycle gas compressor 220 may be disposed on a single driver shaft which may be driven by one electric motor or steam turbine. The ammonia synthesis reactor 230 may in turn discharge ammonia product 234, purge or off gas (not shown) and recycle gas 232, as described above.

[0035] In still further exemplary embodiments, as shown in FIG. 3, the synthesis gas 302 and recycle gas 332 may be combined and compressed in a single synthesis and recycle gas compressor 310. The synthesis and recycle gas compressor 310 may be in one casing and may be driven by one electric motor or steam turbine. The synthesis gas 302 and recycle gas 332 may enter the compressor 310 independently and be combined in compressor 310. According to some embodiments, the recycle gas and synthesis gas may be introduced to the compressor at different stages of compression, based on their prior differences in pressure. For example, the recycle gas may be introduced into the compressor at a later stage of compression.

[0036] The foregoing description and accompanying figures illustrate the principles, preferred embodiments and modes of operation of the invention. However, the invention should not be construed as being limited to the particular embodiments discussed above. Additional variations of the embodiments discussed above will be appreciated by those skilled in the art (for example, features associated with certain configurations of the invention may instead be associated with any other configurations of the invention, as desired).

[0037] Therefore, the above-described embodiments should be regarded as illustrative rather than restrictive. Accordingly, it should be appreciated that variations to those embodiments can be made by those skilled in the art without departing from the scope of the invention as defined by the following claims.