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�������컯��԰��������ʯ�������ֹ�˾�˽��Ļ�����רҵ��ҵ԰������ʯ�������ֹ�˾����װ������ʯ����Ϊԭ�ϵ����30��ֺϳɰ���56������صĴ���װ�ã��ֽ�����·ר���ߣ��ӽ�����·֦��վ�ӹ죬ȫ��22.5km���ڳ������Ͻ��г�Ʒ��ͷ���ؼ���ͷ����Ʒ��ͷ�ȸ۲���ʩ��������̨240t/hú�۹�¯��һ̨30MW�����ַ�����飬�긱��99.6%(���)��Һ��CO25000�֣�������ú�ң�ú����

����2004��11����ʯ�������ֹ�˾��������װ�ý���ԭ��·�ߵĹ��ɸ��죬������������������֦��վ�ṩ����Ȼ����ú������Ŀ�����ڼ�ά����װ�õ���������������Ϊ���30��ֺϳɰ���48������أ����ఱ2���/�꣬�������ɸ���Ԥ����2005��3�����Ͷ����

�������ù��̲��֣�������һ̨220t/h��ú�۹�¯��һ̨30MW�ķ�����飬����Ŀ���б����Ѿ��ϱ���ʯ���ɷݹ�˾��������Ԥ�Ƹ���Ŀ��2005��9�½��ɣ�����Ŀ��ʵʩ��ʹ������װ�ó��������б�ÿ��ܣ���2005����ף�ú������Ŀ�ĸ��칤����������������ú����װ���������Ϊ��Ͷú��Ϊ2000�֣�����¯�����������ɳ��ڣ�H2+CO��Ϊ142000Nm3/h���й�����¯������ɼ���1��

���

H2O

H2

CO

CO2

H2S

N2

Ar

COS

CH4

HCl

NH3

HCN

���%

8.1

25.4

56.7

3.5

1.1

5

0.1

1400ppm

95ppm

50ppm

100ppm

140ppm

װ��Ͷ��������¯����25%���������࣬�ϳɰ�������������39.6���/�꣬����57���/�꣬���ఱԼ6.6���/�ꣻ

������Ҫ���ṩ�ĸ���ƷΪCO2����ú�ҡ�ú������ǡ���������������� ���������ݼ��±�2~5

������2 �ҡ�������Dz�Ʒ���

��Ʒ

����

����(��/��)

����

ѹ��

MPa (G)

�¶�

��

��ע

��ú��

161800

 

 

 

����վ��¯����

ú��

40500

 

 

 

����վ��¯����

��ú��

35070

 

 

 

����¯����

ú��

93520

 

 

 

����¯����

���

5100

��99.8%��W��

 

 

�����װ��

��3�ſ�CO2����

��Ʒ

����

����(Nm3/h)

����(vol)

ѹ��

MPa (G)

�¶ȡ�

��ע

CO2

56349

74.2%CO2

0.014

4

�ſ�

N2

56349

25.8% N2

0.014

4

�ſ�

��4�շ�װ�ò�Ʒ����ָ��

������������

��Ʒ����

����

(Nm3/h)(1)

����(vol)

ѹ��

MPa (G)

�¶ȡ�

��ע

����

12050

��99.6%O2

4.52

23

 

VHP N2

6075

��10ppmO2

8.2

 

 

MP N2

6602

��10ppmO2

3.25

 

 

LP1 N2

2500

��10ppmO2

0.7

 

 

LP2 N2

3625

��10ppmO2

0.46

40

 

Һ��

325

��10ppmO2

0.45

-188

 

�DZ�����

625

��ѹ¶��,-40��

0.7

35

 

��������

500

��ѹ¶��,-40��

0.7

35

 

��󹤿�

��Ʒ

����

����

(Nm3/h)(1)

����(vol)

ѹ��

MPa (G)

�¶ȡ�

��ע

����

12653

��99.6%O2

4.52

23

 

VHP N2

7295

��10ppmO2

8.2

 

 

MP N2

7250

��10ppmO2

3.25

 

 

LP1 N2

4825

��10ppmO2

0.7

 

 

LP2 N2

4000

��10ppmO2

0.46

40

 

Һ��

325

��10ppmO2

0.45

-188

 

�DZ�����

750

��ѹ¶��,-40��

0.7

35

 

��������

750

��ѹ¶��,-40��

0.7

35

 

ע�����в�����λNm3/h��ָ��0����0.1013MPa(A) �����²�������������Ϊ��̬������

������5벲�Ʒ����ָ��

��������������(������)

������������(��ֵ֤)

��Ʒ

����

����

(Nm3/h)

����(vol)

ѹ��MPa (G)

�¶ȡ�

��ע

Һ�

1260

��99.999%Ar

��2ppm O2

��3ppm N2

0.18

-181.8

 

��󹤿�

��Ʒ

����

����

(Nm3/h)

����(vol)

ѹ��

MPa (G)

�¶ȡ�

��ע

Һ�

1350

��99.999%Ar

��2ppm O2

��3ppm N2

0.18

-181.8

 

��Һ������

��Ʒ

����

����

(Nm3/h)

����(vol)

ѹ��

MPa (G)

�¶ȡ�

��ע

Һ�

950

��99.999%Ar

��2ppm O2

��3ppm N2

0.18

-181.8

 

ע�����в�����λNm3/h��ָ��0����0.1013MPa(A) �����²�������������Ϊ��̬������

����ú���͸�����ɺ���̨��¯�ܲ��������������Ϊ700t/h������60000KW��ԭ�е�һ��¯����װ�ü���ز��ֽ����Ա����������Ժ�ķ�չ���ºܶ�ռ䣬���⣬ú�����Ϳշ�װ�õĸ�������ҲΪ���컯��԰����ҵ�Ժ�̼һ��������������ķ�չ�ṩ��������������

The Public Facilities and Resource Status of

Chutian Chemical Industrial Zone

����Chutian Chemical Industrial Zone is a professional chemical industrial park which relies on Hubei Branch of Sinopec Corp. The main device of the company is the large-scale device which produce 300 thousand tons of ammonia per year and 560 thousand tons of urea per year using the naphtha as its material. Now, there is a special railway line integrating Jiaoliu railway from Zhijiang station.The total length is 22.5 kms. There are port facilities at the north bank of the Yangtze River ,such as finished products berth, heavy berth, oil berth, etc; There are two 240 t/h coal powder boilers, one turbo-dynamo of 30 MW. The annual by-products are 500 tons of 99.6%(volume) liquid CO2,  pulrverized fuel ash and some cinder.

����Hubei Branch of Sinopec Corp will carry on transition transform of the raw materials route of the existing device in November, 2004.The natural gas offered by Zhijiang station of Zhongwu line will be used to keep the production of the main device during the construction of the project. The whole transition project will be finished in Match,2005. 300 thousand tons of synthetic ammonia, 480 thousand tons of urea per year and 20 thousand tons of margin synthetic ammonia will be gotten.

����In the public project section, one new fine coal powder boiler of 220t/h and one generating set of 30 MW will be set. The feasibility report has been sent to Sinopec Corp. After examining and approving, it is estimated that the project will be built up in September ,2005. The long cycle running of the reformed device will become possible with the implementation of this project. By the end of 2005, the reforming work of ��coal taking the place of oil�� project will enter the stage of producing as a trial. The designed capacity of the coal gasification device is 2000 tons of coal thrown per day. It is 142000Nm3/h of (H2 +CO) that the designed capacity of the gasification stove is converted to exit. The composition of the gas of the gasification stove is as form 1.

Composition

H2O

H2

CO

CO2

H2S

N2

Ar

COS

CH4

HCl

NH3

HCN

Volume%

8.1

25.4

56.7

3.5

1.1

5

0.1

1400ppm

95ppm

50ppm

100ppm

140ppm

The gasification stove will have 25% margin ability after the device is put into operation. The production capacity of synthetic ammonia will be expanded to 3,960,000 tons per year, 570,000 tons of urea per year and the margin ammonia is about 66,000 tons per year.

����The main by-products which can be offered are CO2, cinder, Sulphur, pure oxygen , pure nitrogen , argon. The concrete data is as the forms 2 -5.

����Form 2    Dust , dreg , sulphur product specification

Products Name

Output

 (ton per year)

Purity

Pressure

MPa(G)

Temperature��

Remarks

Pulrverized fuel ash

161800

 

 

 

Power station boiler by-product

Cinder

40500

 

 

 

Power station boiler by-product

Pulrverized fuel ash

35070

 

 

 

Gasification stove by-product

Cinder

93520

 

 

 

Gasification stove by-product

Sulphur

5100

��99.8%��W��

 

 

Sulphur recovery device

Form 3  To air CO2 parameter

Products Name

Output (Nm3/h)

Purity (vol)

Pressure

MPa (G)

Temperature��

Remarks

CO2

56349

74.2%CO2

0.014

4

To air

N2

56349

25.8% N2

0.014

4

To air

Form 4  The products technical specification of the air separator

����Normal working state:

Products Name

Output (Nm3/h)(1)

Purity (vol)

Pressure

MPa (G)

Temperature��

Remarks

O2

12050

��99.6%O2

4.52

23

 

VHP N2

6075

��10ppmO2

8.2

 

 

MP N2

6602

��10ppmO2

3.25

 

 

LP1 N2

2500

��10ppmO2

0.7

 

 

LP2 N2

3625

��10ppmO2

0.46

40

 

Liquid nitrogen

325

��10ppmO2

0.45

-188

 

Air of the instrument

625

Atmospheric pressure dew point,-40��

0.7

35

 

Air of the factory

500

Atmospheric pressure dew point,-40��

0.7

35

 

The maximum working state

Products Name

Output (Nm3/h)(1)

Purity (vol)

Pressure

MPa (G)

Temperature��

Remarks

O2

12653

��99.6%O2

4.52

23

 

VHP N2

7295

��10ppmO2

8.2

 

 

MP N2

7250

��10ppmO2

3.25

 

 

LP1 N2

4825

��10ppmO2

0.7

 

 

LP2 N2

4000

��10ppmO2

0.46

40

 

Liquid nitrogen

325

��10ppmO2

0.45

-188

 

Air of the instrument

750

Atmospheric pressure dew point,-40��

0.7

35

 

Air of the factory

750

Atmospheric pressure dew point,-40��

0.7

35

 

Note: The output unit (Nm3/h) means that examined having under the condition of 0�� and 0.1013 Mpa , is known as the flow of standard state.

����Form 5  Argon products technical indicator

����Output and purity(District out-of-bounds)

����Normal working state:(Guaranteeing value)

Products Name

Output (Nm3/h)

Purity (vol)

Pressure

MPa (G)

Temperature��

Remarks

Argon of the liquid

1260

��99.999%Ar

��2ppm O2

��3ppm N2

0.18

-181.8

 

The maximum working state

Products Name

Output (Nm3/h)

Purity (vol)

Pressure

����MPa (G)

Temperature��

Remarks

Argon of the liquid

1350

��99.999%Ar

��2ppm O2

��3ppm N2

0.18

-181.8

 

no liquid ammonia operating mode

Products Name

Output (Nm3/h)

Purity (vol)

Pressure

MPa (G)

Temperature��

Remarks

Argon of the liquid

950

��99.999%Ar

��2ppm O2

��3ppm N2

0.18

-181.8

 

The note All the yield unit, Nm3/h,means in 0�� and 0.1013 MPa (A) examining volume flow under the qualification , called the normative flux.

����After the coal taking the place of oil project is finished, the gross output vapour tolerance designed capacity of 3 boilers is for 700 t/h, generate electricity 60000KW, the already existing stove build device and relevant part can be kept, developing and leaving much space after giving , in addition gas generation and air separation equipment redundant ability also offer favorable condition for the enterprises in Hubei Chutian Chemical Industrial Zone developing towards C1 chemical industry and other direction in future.

 

[��Դ�� ֦�������̹�����    2005-5-17]

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